JP2008050724A - Deep drawn moldable paper and method for producing the same - Google Patents

Deep drawn moldable paper and method for producing the same Download PDF

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JP2008050724A
JP2008050724A JP2006229470A JP2006229470A JP2008050724A JP 2008050724 A JP2008050724 A JP 2008050724A JP 2006229470 A JP2006229470 A JP 2006229470A JP 2006229470 A JP2006229470 A JP 2006229470A JP 2008050724 A JP2008050724 A JP 2008050724A
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paper
mass
microcapsule particles
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JP4551374B2 (en
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Akira Honma
彰 本間
Katsuhiko Fukuchi
克彦 福地
Masao Kimura
正夫 木村
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Hokuetsu Paper Mills Ltd
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Abstract

<P>PROBLEM TO BE SOLVED: To produce a thermoformable moldable paper enabling the production of a bulky deep draw molded article having characteristics such as heat insulating property, warmth-keeping property, cushioning property, etc., and also not causing breakage/wrinkles on deep draw-molding of a bulky formed article. <P>SOLUTION: The deep drawn moldable paper which is a foamable and moldable paper capable of being thermally molded, consisting mainly of an N-BKP (needle leaf tree-bleached kraft pulp), a thermoplastic synthetic fiber and expandable microcapsule particles, wherein the moldable paper is a multi-layered paper consisting of a surface layer, a middle layer and a reverse surface layer, having a wood pulp blending ratio of ≥51%, blending 10 to 40 mass% expandable microcapsule particles expanding approximately 4 to 5 folds in diameter and ≥60 folds in volume by heating, based on 100 mass% fibrous layer in the middle layer, the expandable microcapsule particles are not blended in the surface and reverse surface layers or the maximum 10 mass% of the microcapsule particles are blended in the middle layer so as to be less than those in the middle layer, the mixture is dried without foaming the micro capsule particles in the drying process of a papermaking machine, calendared and then wound into a thickness of ≤1 mm. <P>COPYRIGHT: (C)2008,JPO&INPIT

Description

本発明は、合成パルプ、木材パルプ及び熱によって発泡する性質をもつマイクロカプセル粒子を主体として組成される加工性に優れた熱成形可能な深絞り成形用の発泡性成形性紙に関する。この成形性紙は、発泡後に嵩高成形体となる。さらに詳しくは、深絞り成形後に、断熱材、自動車の内装材などの用途で使用され、断熱性、保温性、クッション性などの特性をもつ成形体になる。   The present invention relates to a foamable formable paper for deep-drawing that can be thermoformed and is excellent in processability, which is mainly composed of synthetic pulp, wood pulp, and microcapsule particles having a property of foaming by heat. This formable paper becomes a bulky molded product after foaming. More specifically, after deep drawing, it is used in applications such as heat insulating materials and automobile interior materials, and becomes a molded product having properties such as heat insulating properties, heat retaining properties and cushioning properties.

従来、密度が低く、断熱材や自動車の内装材などの用途で使用されているシートは、発泡スチロールや発泡ポリエチレンなどの高分子ポリマーが、断熱性、保温性に優れ、成形性、加工性、クッション性もよく、安価であるために大量に使用されているが、昨今の環境汚染防止への要望から、自然に分解したり、燃焼したりしても汚染物質の出ない紙などへの転換が進められている。   Conventionally, high density polymer sheets such as foamed polystyrene and foamed polyethylene are used for applications such as heat insulating materials and automotive interior materials, which have low density, and have excellent heat insulation and heat retention, moldability, workability, and cushioning. Although it is good and inexpensive, it is used in large quantities. However, due to recent demands for preventing environmental pollution, it has been converted to paper that does not generate pollutants even if it is naturally decomposed or burned. It is being advanced.

特許文献1は、深絞り適性及び成形体の成型保持性があり、熱プレス成型時の作業性に優れ、不透明性、耐油性、耐水性があり、フランジ部の平坦性が良く、トップシール適性に優れ、耐熱用途ではフィルム貼りを行っても木材パルプの配合率を5 1 重量% 以上としたことによって容器包装リサイクル法で紙として扱われ、高い生産効率で成型品を提供することを目的とし、N−BKP(針葉樹晒しクラフトパルプ)、熱可塑性合成繊維及び填料を主体として組成されており、そして表層、中層、裏層で構成される坪量250g/m以上の多層抄きによって、加工性に優れた熱成型可能な成型紙についての技術が記載されている。しかし、深絞り成形後のその密度は0.5g/cm程度で、密度の高いものであり、断熱性、保温性、クッション性などの特性を持つものではない。 Patent Document 1 has deep drawing suitability and molding holdability, excellent workability during hot press molding, opacity, oil resistance, water resistance, good flatness of the flange, and top seal suitability. For heat-resistant applications, even if a film is applied, the wood pulp content ratio is set to 51% by weight or more so that it can be treated as paper by the Containers and Packaging Recycling Law, and to provide molded products with high production efficiency. , N-BKP (softwood bleached kraft pulp), are compositions mainly of thermoplastic synthetic fibers and filler, and the surface layer, middle layer, the basis weight of 250 g / m 2 or more multilayer paper making consists of backing layer, processing A technology for thermoforming molding paper having excellent properties is described. However, the density after deep drawing is about 0.5 g / cm 3 , which is a high density and does not have properties such as heat insulating properties, heat retaining properties, and cushioning properties.

特許文献2は、低密度体で、断熱性、保温性、耐衝撃性、クッション性等に優れた発泡体粒子混抄紙の提供を目的とし、天然パルプ100重量部に対して発泡性粒子を3〜20重量部添加し、混抄させ、加熱乾燥時に発泡することによって、密度0.1〜0.3g/cmの混抄紙を製造する方法が、示されているが、この場合、その成形性は十分ではなく、成形時に大きな伸びを要求される深絞りの成形を行う時に混抄紙が破断したり、混抄紙に皺がでたりして、深絞り成形を行うことが出来ない。 Patent Document 2 aims to provide a foam particle mixed paper that is a low-density body and excellent in heat insulation, heat retention, impact resistance, cushioning properties, and the like. Although a method for producing a mixed paper having a density of 0.1 to 0.3 g / cm 3 by adding ~ 20 parts by weight, mixing and foaming during heating and drying is shown, in this case, the formability thereof is shown. Is not sufficient, and when performing deep drawing, which requires a large elongation during forming, the mixed paper breaks or wrinkles on the mixed paper, making it impossible to perform deep drawing.

特許文献3は、特許文献2と同様に低密度体で、断熱性、保温性、耐衝撃性、クッション性等に優れた発泡体粒子混抄紙の提供を目的とし、天然パルプ50重量%以上で、他に合成パルプを配合した繊維層に対して、発泡性粒子を3〜20重量部添加し、混抄させ、密度0.1〜0.3g/cmの混抄紙を製造する方法が示されている。この文献の混抄紙の場合にも、大きな伸びを要求される深絞りの成型を行う場合には混抄紙が破断したり、混抄紙に皺がでたりして、深絞り成型を行うことが出来ない。 Patent Document 3 aims to provide a foam particle mixed paper which is a low-density body and has excellent heat insulating properties, heat retaining properties, impact resistance, cushioning properties, etc., as in Patent Document 2, and the natural pulp is 50% by weight or more. In addition, 3 to 20 parts by weight of expandable particles are added to the fiber layer containing synthetic pulp and mixed to produce a mixed paper having a density of 0.1 to 0.3 g / cm 3. ing. Even in the case of the blended paper of this document, when performing deep drawing that requires large elongation, the mixed paper can break or wrinkle on the mixed paper, and deep drawing can be performed. Absent.

特開2006−022439号公報JP 2006-022439 A 特許第3024591号公報Japanese Patent No. 3024591 特許第3166763号公報Japanese Patent No. 3166663

以上に述べた通り、断熱性、保温性、クッション性などの特性をもつ嵩高深絞り成形体を、従来技術の様な問題を生じることなく製造することを可能とする熱成形可能な深絞り成形性紙を造る従来の技術は存在していない。   As mentioned above, deep-drawing that can be thermoformed to produce bulky deep-drawn molded products with properties such as heat insulation, heat retention, cushioning, etc. without causing problems as in the prior art There is no conventional technique for producing a quality paper.

本発明の目的は、断熱性、保温性、クッション性などの特性をもつ嵩高い深絞り成形体を製造することを可能とする熱成形可能な成形性紙を通常の抄紙機を用いて製造し、しかも、嵩高成形体に深絞り成形を行うときに、破断・皺の発生のない該深絞り成形性紙を提供することである。また、本発明の目的は、耐熱用途で、フィルムを貼っても、木材パルプの配合率が51質量%以上としたことによって、容器包装リサイクル法で紙として取り扱われる成形性紙を提供することである。   An object of the present invention is to produce a thermoformable formable paper using an ordinary paper machine that makes it possible to produce a bulky deep-drawn molded product having properties such as heat insulation, heat retention, and cushioning properties. Moreover, it is an object of the present invention to provide the deep-drawn formable paper that is free from breakage and wrinkles when deep drawing is performed on a bulky formed body. In addition, the object of the present invention is to provide a formable paper that can be handled as paper by the Containers and Packaging Recycling Law, even when a film is pasted, for a heat resistant application, by setting the blending ratio of wood pulp to 51% by mass or more. is there.

本発明者は、成形性、リサイクル性の点から検討を重ねた結果、N−BKP(針葉樹晒しクラフトパルプ)、熱可塑性合成繊維及び発泡性マイクロカプセル粒子を主体として組成される熱成形可能な発泡性成形性紙を多層で構成し、主として中間層に発泡性マイクロカプセルを混抄した場合に、驚くべきことに上記の課題が解決できることを見出した。   As a result of repeated investigations from the viewpoint of moldability and recyclability, the present inventor has conducted thermoforming foaming composed mainly of N-BKP (softwood bleached kraft pulp), thermoplastic synthetic fibers, and foamable microcapsule particles. It has been found that the above-mentioned problem can be solved surprisingly when the formable paper is composed of multiple layers and foamed microcapsules are mainly mixed in the intermediate layer.

すなわち本発明は、N−BKP(針葉樹晒しクラフトパルプ)、熱可塑性合成繊維及び発泡性マイクロカプセル粒子を主体として組成される熱成形可能な発泡性成形性紙において、該成形性紙が表層、少なくとも1層の中層、裏層で構成される木材パルプ配合率51%以上の多層抄き紙であり、該中層に繊維層100質量%当たり、加熱によってその直径が約4〜5倍及び体積が60倍以上に膨張する発泡性マイクロカプセル粒子を10〜40質量%配合し、表層および裏層には該発泡性マイクロカプセル粒子を配合しないかまたは中層よりも少なく最大10質量%配合し、抄紙機の乾燥工程で、該発泡性マイクロカプセル粒子を発泡させずに乾燥後、キャレンダーに掛け、厚さ1mm以下で巻き取ることを特徴とする深絞り成形性紙に関する。   That is, the present invention relates to a thermoformable foamable formable paper composed mainly of N-BKP (softwood bleached kraft pulp), thermoplastic synthetic fibers and expandable microcapsule particles, wherein the formable paper is at least a surface layer. It is a multilayer paper having a wood pulp blending ratio of 51% or more, consisting of one middle layer and a back layer. The diameter of the middle layer is about 4 to 5 times and the volume is 60 times per 100 mass% of the fiber layer by heating. 10 to 40% by mass of expandable microcapsule particles that expand more than twice, and the surface layer and the back layer are not compounded with the expandable microcapsule particles or less than the middle layer and are compounded up to 10% by mass. In a drying process, the foamable microcapsule particles are dried without being foamed, then applied to a calendar, and taken up to a thickness of 1 mm or less, and the deep-drawn formable paper .

本発明の一つの実施形態においては、成形性紙の表裏層に前記発泡性マイクロカプセル粒子を繊維層100質量%当たり1〜10質量%添加し、前記多層抄き紙全体としての繊維層100質量%当たり、該発泡性マイクロカプセル粒子が9〜35質量%になることを特徴とする深絞り成形性紙に関するものである。 In one embodiment of the present invention, the foamable microcapsule particles are added to the front and back layers of the formable paper in an amount of 1 to 10% by mass per 100% by mass of the fiber layer, and the mass of the fiber layer is 100% by mass as the entire multilayer paper. The present invention relates to a deep-drawn formable paper characterized in that the expandable microcapsule particles are 9 to 35% by mass per%.

本発明の一つの有利な実施形態においては、熱可塑性合成繊維が、融点100〜180℃である多分岐状ポリエチレン系合成パルプであることを特徴とする深絞り成形性紙に関する。   In one advantageous embodiment of the invention, the invention relates to a deep-drawn formable paper characterized in that the thermoplastic synthetic fiber is a multi-branched polyethylene synthetic pulp having a melting point of 100-180 ° C.

本発明の一つの有利な実施形態においては、前記深絞り成形性紙において、添加した発泡性マイクロカプセル粒子を、100〜220℃の加熱によって、直径が約4〜5倍、体積が60倍以上に膨張させ、発泡性マイクロカプセル粒子の含有量に依存してかつ使用目的に応じて、未発泡の多層抄き紙の厚さの好ましくは4〜8倍、特に好ましくは4〜6倍の厚さに発泡膨張させることを特徴とする深絞り成形性紙に関するものである。   In one advantageous embodiment of the present invention, in the deep-drawn paper, the expandable microcapsule particles added are about 4 to 5 times in diameter and 60 or more times in volume by heating at 100 to 220 ° C. Depending on the content of the expandable microcapsule particles and depending on the intended use, the thickness of the unfoamed multilayer paper is preferably 4 to 8 times, particularly preferably 4 to 6 times the thickness. The present invention relates to a deep-drawn formable paper characterized by being foamed and expanded.

本発明の一つの有利な実施態様においては、耐熱用途のために、成形性紙の表面をポリエチレンフィルム、ポリプロピレンフィルム、ポリエステルフィルム、ポリブチレンテレフタレートフィルム、ポリメチルペンテンフィルムでラミネート加工してもよい。   In one advantageous embodiment of the invention, the surface of the formable paper may be laminated with a polyethylene film, polypropylene film, polyester film, polybutylene terephthalate film, polymethylpentene film for heat resistant applications.

本発明の一つの有利な実施形態においては、深絞り成形性紙の発泡方法として、乾燥したシートを熱プレス成形にて、目的の厚さのクリアランスを開けて温度100〜220℃で加熱発泡させ、その後で深絞り成形する方法がある。   In one advantageous embodiment of the present invention, as a method of foaming deep-drawn formable paper, the dried sheet is heated and foamed at a temperature of 100 to 220 ° C. with a clearance of the desired thickness by hot press molding. Then, there is a method of deep drawing.

また、本発明の深絞り成形性紙を、そのまま深絞り成形機に入れ、目的の厚さのクリアランスを開けて温度100〜220℃で直接的に加熱成形する方法もある。   Further, there is also a method in which the deep-drawn formable paper of the present invention is directly put into a deep-drawing machine and directly formed by heating at a temperature of 100 to 220 ° C. with a clearance of a desired thickness.

本発明の一つの有利な実施形態においては、前記成形性紙の発泡後の密度が、0.1g/cm未満であることを特徴とする深絞り成形体に関する。 In one advantageous embodiment of the present invention, the present invention relates to a deep-drawn molded article, wherein the formable paper has a density after foaming of less than 0.1 g / cm 3 .

本発明の成形性紙は、木材パルプ、熱可塑性合成繊維及び発泡性マイクロカプセル粒子を組み合わせる構成によって、深絞りの成形を行うときに、破断・皺の発生なく深絞り成形可能であり、厚さ1mm以下であるためにリールでの巻き取りで皺や折れが発生せず、発泡ムラも発生せず、発泡後または深絞り成形後に断熱性、保温性、クッション性などの特性をもたせた機能性の高い、かつ、容器包装リサイクル法で紙として取り扱われる分野で、従来ではできなかった熱成形可能な0.1g/cm未満の低密度の成形体を提供することが可能となった。 The formable paper of the present invention can be deep-drawn without breakage or wrinkles when deep-drawn by using a combination of wood pulp, thermoplastic synthetic fibers, and expandable microcapsule particles. Since it is 1 mm or less, it does not cause wrinkles or folds when wound on a reel, does not cause foaming unevenness, and has functions such as heat insulation, heat retention, and cushioning after foaming or after deep drawing. It has become possible to provide a low-density molded body of less than 0.1 g / cm 3 that can be thermoformed in a field that is high and that is handled as paper by the Containers and Packaging Recycling Law.

本発明は、木材パルプと熱可塑性合成繊維と発泡性マイクロカプセル粒子とを混抄した熱成形可能な多層抄き成形性紙である。   The present invention is a thermoformable multi-layer formable paper in which wood pulp, thermoplastic synthetic fiber, and expandable microcapsule particles are mixed.

本発明における熱可塑性合成繊維であるポリオレフィン系合成パルプとしては、汎用の抄紙機による湿式抄造プロセスに適した、多分岐状の繊維性状を有するポリエチレン又はポリプロピレンからなるポリオレフィン系合成パルプが好ましい。また、成形時の加熱によって木材パルプとの熱溶融による接着性に優れるものが好ましく、融点が100〜180℃のポリオレフィン系の合成パルプが安価であり、好適に用いられる。例えば、三井化学(株)からSWPの商品名で市販されているものを使用できるが、本発明はこのSWPに限定されるものではない。   The polyolefin synthetic pulp which is a thermoplastic synthetic fiber in the present invention is preferably a polyolefin synthetic pulp made of polyethylene or polypropylene having a multi-branched fiber property suitable for a wet papermaking process using a general-purpose paper machine. Moreover, what is excellent in the adhesiveness by heat fusion with a wood pulp by the heating at the time of shaping | molding is preferable, and the polyolefin-type synthetic pulp whose melting | fusing point is 100-180 degreeC is cheap, and is used suitably. For example, what is marketed under the trade name SWP from Mitsui Chemicals, Inc. can be used, but the present invention is not limited to this SWP.

これらのポリオレフィン系合成パルプの形態は、抄紙機で抄紙できる範囲であれば短繊維でも長繊維でもよいが、その平均繊維長として0.1〜10mmの範囲内であることが好ましい。0.1mm未満では、繊維間の絡み合いが少なく実質的にシート状にすることが難しく、10mmを超えると抄紙で、均一なシートにすることが難しい。   The form of these polyolefin-based synthetic pulps may be short fibers or long fibers as long as they can be made by a paper machine, but the average fiber length is preferably in the range of 0.1 to 10 mm. If it is less than 0.1 mm, it is difficult to form a sheet substantially with little entanglement between the fibers, and if it exceeds 10 mm, it is difficult to make a uniform sheet by papermaking.

本発明で使用する木材パルプとしては、主にN−BKP(針葉樹晒クラフトパルプ)に代表される木材漂白化学パルプが使用される。必要に応じてL−BKP(広葉樹晒クラフトパルプ)、GP(砕木パルプ)、TMP(サーモメカニカルパルプ)、BCTMP(晒ケミサーモメカニカルパルプ)などの機械パルプ、古紙パルプを適宜配合する事も出来る。   As the wood pulp used in the present invention, wood bleached chemical pulp typified by N-BKP (conifer bleach bleached kraft pulp) is mainly used. If necessary, mechanical pulp such as L-BKP (hardwood bleached kraft pulp), GP (crushed wood pulp), TMP (thermomechanical pulp), BCTMP (bleached chemithermomechanical pulp) and the like can be appropriately blended.

本発明の成形性紙における熱可塑性合成繊維と木材パルプとの配合率は、表層、裏層と中層では異なっていてもよい。適正な配合率は、熱成形時の深絞り適性、成形体の形状安定性、作業性などを加味しながら予備実験によって容易に決定できる。   The blending ratio of the thermoplastic synthetic fiber and the wood pulp in the formable paper of the present invention may be different between the front layer, the back layer and the middle layer. An appropriate blending ratio can be easily determined by a preliminary experiment while taking into account deep drawing suitability during thermoforming, shape stability of the molded body, workability, and the like.

本発明の成形性紙における熱可塑性合成繊維の配合率は、表層、裏層においては、0〜30質量%、好ましくは、10〜25質量%とする。30質量%以上では、熱成形加工時に金型に融着しやすくなり、離型性が劣る。また、中層においては30〜100質量%、好ましくは40〜90質量%、更に好ましくは、45〜85重量%とする。30質量%未満では、熱成形加工後の深絞り適性及び成形体の形状安定性が劣る。また、全層として、木材パルプの配合率を51質量%以上とするような配合率が好ましい。   The blending ratio of the thermoplastic synthetic fiber in the formable paper of the present invention is 0 to 30% by mass, preferably 10 to 25% by mass in the surface layer and the back layer. If it is 30% by mass or more, it becomes easy to fuse to the mold during thermoforming, and the releasability is poor. Moreover, in a middle layer, it is 30-100 mass%, Preferably it is 40-90 mass%, More preferably, you may be 45-85 weight%. If it is less than 30% by mass, the suitability for deep drawing after thermoforming and the shape stability of the molded product are poor. Moreover, the mixture rate which makes the mixture rate of a wood pulp 51 mass% or more as a whole layer is preferable.

本発明の成形性紙に使用する発泡性マイクロカプセル粒子は、マイクロカプセル内に低沸点溶剤を封入した熱膨張性マイクロカプセルで、80〜220℃の温度で、短時間の加熱によってその直径が4〜5倍及び体積が60倍以上に膨張する平均径が5〜40μmの粒子である。低沸点溶剤としては、イソブタン、ペンタン、石油エーテル、ヘキサン、低沸点ハロゲン化炭化水素、メチルシランなどの揮発性有機溶剤を塩化ビニリデン、アクリロニトリル、アクリル酸エステル、メタクリル酸エステルなどの共重合体から成る熱可塑性樹脂で包み込んだものである。これらの発泡性マイクロカプセル粒子として、例えばエクスパンセルDU、同WUF(スウェーデン製、販売元日本フィライト(株))が使用できるが、本発明はこのエクスパンセルDU、同WUFに限定されるものではない。   The expandable microcapsule particles used in the formable paper of the present invention are thermally expandable microcapsules in which a low-boiling solvent is enclosed in a microcapsule, and the diameter thereof is 4 by heating at a temperature of 80 to 220 ° C. for a short time. Particles having an average diameter of 5 to 40 μm that expand to 5 times and a volume of 60 times or more. Low boiling solvents include volatile organic solvents such as isobutane, pentane, petroleum ether, hexane, low boiling halogenated hydrocarbons, and methylsilane, and heat composed of copolymers such as vinylidene chloride, acrylonitrile, acrylic esters, and methacrylic esters. Wrapped with plastic resin. As these expandable microcapsule particles, for example, Expandel DU and WUF (made in Sweden, sold by Nihon Philite Co., Ltd.) can be used, but the present invention is limited to these Expandel DU and WUF. is not.

発泡性マイクロカプセル粒子の配合量は、成形性紙の中層繊維層100質量部%当たり、10〜40質量%、好ましくは10〜38質量%であり、より好ましくは10〜35質量%である。10質量%未満では、密度が高くなり、断熱性、保温性およびクッション性が低下し、40質量%を超えると、経済性の面から、あまり適当とはいえない。また、表裏層に入れる場合は、表裏層の繊維層100質量部%当たり、最大10質量%、好ましくは最大9質量%、特に好ましくは8質量%配合し、その量は中層の発泡性マイクロカプセル粒子の配合量よりも少ない。表裏層の該粒子配合量が10質量%より多いと、深絞り成形時に成形体に皺が発生する恐れがある。成形性紙の繊維層全体に対して9〜35質量%配合する。成形性紙の繊維全体に対する発泡性マイクロカプセルの配合量が9質量%未満であると、発泡量が少な過ぎて十分な断熱性、保温性およびクッション性を達成できず、35質量%を超える場合には十分な強度の紙を得ることができない。   The blending amount of the expandable microcapsule particles is 10 to 40% by mass, preferably 10 to 38% by mass, and more preferably 10 to 35% by mass per 100 parts by mass of the middle fiber layer of the formable paper. If it is less than 10% by mass, the density becomes high, and the heat insulating property, the heat retaining property and the cushioning property are deteriorated. If it exceeds 40% by mass, it is not very suitable from the viewpoint of economy. In addition, when it is put in the front and back layers, it is blended in a maximum of 10% by weight, preferably a maximum of 9% by weight, particularly preferably 8% by weight, per 100 parts by weight of the fiber layer of the front and back layers, and the amount thereof is the foamable microcapsule of the middle layer. Less than the amount of particles. If the amount of the particles in the front and back layers is more than 10% by mass, wrinkles may occur in the molded body during deep drawing. 9-35 mass% is mix | blended with respect to the whole fiber layer of a formable paper. When the blending amount of the foamable microcapsule with respect to the whole fiber of the formable paper is less than 9% by mass, the foaming amount is too small to achieve sufficient heat insulation, heat retention and cushioning properties, and exceeds 35% by mass. Therefore, it is not possible to obtain a sufficiently strong paper.

本発明の成形性紙中には、前記パルプ、発泡性マイクロカプセル粒子の他に、本発明の目的効果を損なわない範囲で、一般的に使用されている各種の歩留り向上剤、紙力向上剤、内添サイズ剤、ピッチコントロール剤、消泡剤などの薬品類を適宜使用できる。   In the formable paper of the present invention, in addition to the pulp and expandable microcapsule particles, various yield improvers and paper strength improvers that are generally used within a range that does not impair the object effects of the present invention. Further, chemicals such as an internal sizing agent, a pitch control agent, and an antifoaming agent can be used as appropriate.

本発明の成形性紙は、長網抄紙機、円網抄紙機、長網と円網のコンビネーションマシンなどの一般的な多層抄き抄紙機によって製造される。   The formable paper of the present invention is produced by a general multi-layer paper machine such as a long paper machine, a circular paper machine, and a long net and circular net combination machine.

また、本発明の成形性紙にサイズプレス、ゲートロールなどの塗工方法にて、紙の表面に澱粉、ポリビニルアルコール、表面サイズ剤、蛍光増白剤などを塗布することも可能である。   It is also possible to apply starch, polyvinyl alcohol, a surface sizing agent, a fluorescent whitening agent, etc. to the surface of the paper by a coating method such as a size press or a gate roll on the formable paper of the present invention.

本発明の成形性紙の坪量は、特に限定するものではないが通常200〜600g/m程度の範囲である。 The basis weight of the formable paper of the present invention is not particularly limited, but is usually in the range of about 200 to 600 g / m 2 .

発泡処理前の乾燥方法としては、特に限定されるものではなく、通常のシリンダードライヤーなどにおいて、発泡性マイクロカプセル粒子が発泡しない70℃以下での乾燥が必要である。   The drying method before the foaming treatment is not particularly limited, and it is necessary to dry at 70 ° C. or less where foamable microcapsule particles do not foam in a normal cylinder dryer or the like.

本発明の成形性紙のカレンダー処理は、紙厚の均一化と共に抄紙機で巻き取れる厚さに処理する目的で行われる。その厚さは、1mm以下である。カレンダー処理は、オンマシンで配置されているマシンカレンダー、その他にスーパーカレンダー、グロスカレンダー、ブラッシカレンダー、マットカレンダー、ソフトカレンダーなどを用いることができ、カレンダーの種類は、特に限定されるものではない。   The calendering of the formable paper of the present invention is performed for the purpose of processing the paper to a thickness that can be taken up by a paper machine while making the paper thickness uniform. Its thickness is 1 mm or less. For the calendar processing, a machine calendar arranged on-machine, a super calendar, a gloss calendar, a brush calendar, a mat calendar, a soft calendar, and the like can be used. The type of calendar is not particularly limited.

本発明の成形性紙の発泡方法の一つとして、巻き取られた発泡前の成形性紙を所定の大きさに断裁し、これを熱プレスなどの加熱プレス機での深絞り成形により、目的の厚さのクリアランスで、上下からプレス加熱する方法が挙げられる。その際の密度は特に限定されないが、低密度であるのが望ましく、特に0.06〜0.13g/cmであることが望ましい。密度が、0.13g/cmより多い場合、発泡量が不十分であり、発泡成形体の断熱性、保温性、クッション性などの特性が失われる恐れがある。 As one of the foaming methods of the formable paper of the present invention, the wound formable paper before foaming is cut into a predetermined size, and this is performed by deep drawing with a hot press machine such as a hot press. There is a method of press heating from above and below with a clearance of a certain thickness. Although the density in that case is not specifically limited, It is desirable that it is a low density, and it is desirable that it is 0.06-0.13 g / cm < 3 > especially. When the density is higher than 0.13 g / cm 3 , the foaming amount is insufficient, and the foam molded article may lose characteristics such as heat insulation, heat retention, and cushioning properties.

発泡方法のもう一つの方法として、目的の大きさに打ち抜き、成形機で加工する際に、成形機にて、所定の厚さで成形し、加熱発泡する方法が挙げられるが、成形時間が長く、成形効率が低下する恐れがある。   Another method of foaming is a method of punching to a desired size and processing with a molding machine, molding with a molding machine at a predetermined thickness, and heating and foaming, but the molding time is long. There is a risk that the molding efficiency is lowered.

実施例:
本発明を実施例によって、更に詳細に説明するが、本発明は、勿論これに限定されるものではない。なお、特に断らない限り、例中の部、添加%は固形分換算での質量部または、質量%である。
Example:
The present invention will be described in more detail with reference to examples, but the present invention is not limited thereto. In addition, unless otherwise indicated, the part and addition% in an example are a mass part or mass% in conversion of solid content.

<成形性紙の製造>
表裏層として、N−BKP/SWP(三井化学社製、E620、融点135℃の多分岐状ポリエチレン系合成パルプ)=70/30%配合のパルプを混合し、カナディアンスタンダードフリーネス(以下「フリーネス」と略す。)500mlのパルプスラリーを得、内添サイズ剤としてロジン系エマルジョン(星光PMC社製、AL−120)を対パルプ0.3%、硫酸バンドを対パルプ1%、カチオン化澱粉(日本食品化工社製、ネオタック40T)を対パルプ1%添加し、丸網抄紙機にて、表裏層の目標坪量を90g/mとした。中層として、N−BKP/SWP(三井化学社製、E620)=50/50%配合し、フリーネス500mlのパルプスラリーとし、この繊維層100質量%当たり、発泡性マイクロカプセル粒子としてエクスパンセル930−120DU(スウェーデン製、販売元日本フィライト(株))25質量%を添加し、内添サイズ剤としてロジン系エマルジョン(星光PMC社製、AL−120)を対パルプ0.3%、硫酸バンドを対パルプ1%、カチオン化澱粉(日本食品化工社製、ネオタック40T)を対パルプ1%添加し、丸網抄紙機にて、2つの中層の目標坪量をそれぞれ135g/mとし、4層抄き合わせによって目標坪量450g/mにて紙を抄紙し、ドライヤーにて70℃で乾燥し、キャレンダーを掛け、厚さ1mmにてリールで巻き取り、発泡性マイクロカプセル粒子を発泡させていない成形性紙を製造した。
<Manufacture of formable paper>
As front and back layers, N-BKP / SWP (manufactured by Mitsui Chemicals, E620, multi-branched polyethylene synthetic pulp having a melting point of 135 ° C.) = 70/30% pulp was mixed, and Canadian Standard Freeness (hereinafter “Freeness”) Abbreviated.) 500 ml of pulp slurry was obtained, and rosin-based emulsion (AL-120 manufactured by Seiko PMC Co., Ltd., AL-120) as an internal sizing agent was 0.3% of pulp, sulfate band was 1% of pulp, and cationized starch (Japanese food) 1% of Neotac 40T manufactured by Kako Co., Ltd. was added, and the target basis weight of the front and back layers was set to 90 g / m 2 with a round net paper machine. As an intermediate layer, N-BKP / SWP (Mitsui Chemical Co., Ltd., E620) = 50/50% is blended to form a freeness 500 ml pulp slurry, and EXPANSEL 930- is used as expandable microcapsule particles per 100% by mass of the fiber layer. 120 DU (made in Sweden, Nihon Philite Co., Ltd.) 25% by mass was added, and rosin emulsion (manufactured by Seiko PMC, AL-120) was used as an internal sizing agent. Add 1% of pulp and 1% of cationized starch (Neotac 40T, manufactured by Nippon Shokuhin Kako Co., Ltd.) to pulp, and set the target basis weight of the two middle layers to 135g / m 2 on a round net paper machine. paper making paper by the target basis weight 450 g / m 2 by alignment can, dried at 70 ° C. at drier, multiplied by calendering, Lee at 1mm thick Wound in, to produce the moldability paper that has not been foamed expandable microcapsule particles.

<発泡させた嵩高成形体の調整>
上記の発泡前の成形性紙を縦20cm×横20cmの大きさに断裁し、熱プレス(ミニテストプレス−10、東洋精機社製)を用い、クリアランス6mmで、プレス上下の温度200℃にて、一分間プレスし、発泡性マイクロカプセル粒子を発泡させた嵩高成形体を得た。
<Adjustment of foamed bulky molded product>
The formable paper before foaming is cut into a size of 20 cm in length and 20 cm in width, and a heat press (Mini Test Press-10, manufactured by Toyo Seiki Co., Ltd.) is used with a clearance of 6 mm and a temperature above and below the press of 200 ° C. , And pressed for 1 minute to obtain a bulky molded product obtained by foaming expandable microcapsule particles.

本発明の実施例における坪量、厚さ及び密度は、次のJISに従い、発泡ムラの有無、金型成形性については、目視で評価した。   The basis weight, thickness, and density in the examples of the present invention were visually evaluated for the presence or absence of uneven foaming and moldability in accordance with the following JIS.

a.坪量:JIS P 8124
b.厚さ、密度:JIS P 8118
c.発泡ムラ:目視にて評価
○:発泡ムラなし、実用レベルにある。
△:発泡ムラ幾分あり、実用に耐えない。
×:発泡ムラあり、実用に耐えない。
d.深絞り成形性:深さ10mmのトレイ成形機を用いて、雄雌金型をセットし温度(180±5)℃、プレス圧50kg/cm、クリアランス5mm、プレス時間10秒で連続成形を行い、材料破壊、皺発生の有無などの深絞り適性及び成形体の形状安定性を総合して評価した。
○:良好で、実用レベルにある。
△:やや劣り、実用に耐えない。
×:劣り、実用に耐えない。
a. Basis weight: JIS P 8124
b. Thickness and density: JIS P 8118
c. Foaming unevenness: Visual evaluation ○: No foaming unevenness, at practical level.
Δ: Some foaming unevenness is not practical.
X: There is foaming unevenness and it cannot endure practical use.
d. Deep drawability: Using a tray molding machine with a depth of 10 mm, male and female dies are set, and continuous molding is performed at a temperature (180 ± 5) ° C., a press pressure of 50 kg / cm 2 , a clearance of 5 mm, and a press time of 10 seconds. In addition, deep drawing aptitude such as material destruction and wrinkle generation and shape stability of the molded body were comprehensively evaluated.
○: Good and practical level.
Δ: Slightly inferior and not practical.
X: Inferior and not practical.

実施例1の表裏層に繊維層100質量%当たり、発泡性マイクロカプセル粒子としてエクスパンセル007−40WUF(スウェーデン製、販売元日本フィライト(株))3.5質量%を添加した以外は、実施例1と同様にして、4層抄き合わせによって坪量450g/mにて紙を抄紙し、ドライヤーにて70℃で乾燥し、リールで巻き取り、発泡性マイクロカプセル粒子を発泡させていない成形性紙を得、実施例1と同様に熱プレスにて、発泡性マイクロカプセル粒子を発泡させた嵩高成形体を得た。 Except for adding 100% by mass of EXPANCEL 007-40WUF (made by Sweden, distributor Nihon Philite Co., Ltd.) as expandable microcapsule particles to the front and back layers of Example 1 per 100% by mass of the fiber layer. In the same manner as in Example 1, paper was made at a basis weight of 450 g / m 2 by four-layer making, dried at 70 ° C. with a dryer, wound on a reel, and foamed microcapsule particles were not foamed. A formable paper was obtained, and a bulky molded body in which foamable microcapsule particles were foamed was obtained by hot pressing in the same manner as in Example 1.

実施例1の原紙において、中層に繊維層100質量%当たり、発泡性マイクロカプセル粒子としてエクスパンセル930−120DU(スウェーデン製、販売元日本フィライト(株))30質量%を添加した以外は実施例1と同様にして、4層抄き合わせによって目標坪量450g/mにて紙を抄紙し、ドライヤーにて70℃で乾燥し、リールで巻き取り、発泡性マイクロカプセル粒子を発泡させていない成形性紙を得、実施例1と同様に熱プレスにて、発泡性マイクロカプセル粒子を発泡させた嵩高成形体を得た。 In the base paper of Example 1, Example except that 30% by mass of EXPANSEL 930-120DU (manufactured by Sweden Philharmonic Co., Ltd.) was added as expandable microcapsule particles per 100% by mass of the fiber layer in the middle layer. In the same manner as in No. 1, paper is made at a target basis weight of 450 g / m 2 by four-layer making, dried at 70 ° C. with a dryer, wound on a reel, and foamed microcapsule particles are not foamed. A formable paper was obtained, and a bulky molded body in which foamable microcapsule particles were foamed was obtained by hot pressing in the same manner as in Example 1.

比較例1Comparative Example 1

実施例1において、中層に繊維層100質量%当たり、発泡性マイクロカプセル粒子としてエクスパンセル930−120DU(スウェーデン製、販売元日本フィライト(株))9質量%を添加した以外は実施例1と同様にして、4層抄き合わせによって目標坪量450g/mにて紙を抄紙し、ドライヤーにて70℃で乾燥し、リールで巻き取り、発泡性マイクロカプセル粒子を発泡させていない成形性紙を得、実施例1と同様に熱プレスにて、発泡性マイクロカプセル粒子を発泡させた嵩高成形体を得た。 Example 1 is the same as Example 1 except that 9% by mass of EXPANSEL 930-120DU (made by Sweden, distributor Nihon Philite Co., Ltd.) is added as expandable microcapsule particles per 100% by mass of the fiber layer in the middle layer. In the same manner, paper having a target basis weight of 450 g / m 2 is made by four-layer making, dried at 70 ° C. with a dryer, wound with a reel, and foamable microcapsule particles are not foamed. Paper was obtained, and a bulky molded body in which foamable microcapsule particles were foamed was obtained by hot pressing in the same manner as in Example 1.

比較例2Comparative Example 2

実施例1において、ドライヤーにて70℃で乾燥し、キャレンダーを掛けずに、厚さ1.5mmにて、リールで巻き取り、発泡性マイクロカプセル粒子を発泡させていない成形性紙を得、実施例1と同様に熱プレスにて、発泡性マイクロカプセル粒子を発泡させた嵩高成形体を得た。   In Example 1, dried at 70 ° C. with a dryer, wound with a reel at a thickness of 1.5 mm without applying a calendar, to obtain a formable paper without foaming the foamable microcapsule particles, A bulky molded body obtained by foaming expandable microcapsule particles was obtained by hot pressing in the same manner as in Example 1.

比較例3Comparative Example 3

実施例1において、表裏層のN−BKP/SWP(三井化学社製、E620)=50/50%配合のパルプを混合した以外は実施例1と同様にして、4層抄き合わせによって目標坪量450g/mにて紙を抄紙し、ドライヤーにて70℃で乾燥し、リールで巻き取り、発泡性マイクロカプセル粒子を発泡させていない成形性紙を得、実施例1と同様に熱プレスにて、発泡性マイクロカプセル粒子を発泡させた嵩高成形体を得た。 In Example 1, N-BKP / SWP (Mitsui Chemical Co., Ltd., E620) = 50/50% blended pulp of the front and back layers was mixed in the same manner as in Example 1 except that the target basis weight was obtained by combining the four layers. Paper is made at an amount of 450 g / m 2 , dried at 70 ° C. with a dryer, wound with a reel to obtain a formable paper in which the foamable microcapsule particles are not foamed, and hot-pressed as in Example 1. Thus, a bulky molded body obtained by foaming expandable microcapsule particles was obtained.

これらの結果を表1に示す。   These results are shown in Table 1.

Figure 2008050724
Figure 2008050724

表の結果及び実施例から明らかなように、本発明の成形性紙は、木材パルプと熱可塑性合成繊維と発泡性マイクロカプセル粒子とを主体にした多層抄き板紙において、木材パルプ配合率が全層として51質量%以上、発泡性マイクロカプセル粒子が繊維層に対し、9〜35質量%である熱成形可能な成形性紙を製造することによって、比較的に密度が低く、断熱性、保温性、クッション性などの特性をもち、深絞り成形性を備えた成形性紙を提供することを可能とした。また、木材パルプの配合率を51質量%以上としたことによって、容器包装リサイクル法で、紙として取り扱われる。   As is clear from the results of the table and the examples, the formable paper of the present invention is a multilayer paperboard mainly composed of wood pulp, thermoplastic synthetic fibers, and expandable microcapsule particles, and the wood pulp content is all. By producing a formable paper that is 51% by mass or more and the foamable microcapsule particles are 9 to 35% by mass with respect to the fiber layer as a layer, the density is relatively low, and the heat insulation and heat retention It was possible to provide a formable paper having characteristics such as cushioning properties and deep drawability. Moreover, by setting the blending ratio of wood pulp to 51% by mass or more, it is handled as paper by the Containers and Packaging Recycling Law.

詳細には、比較例1の中層の発泡剤の配合率が9%においては、発泡後の厚さが3.2mm(3.2倍)と発泡量が少なくかつ密度0.156g/cmと高いために、断熱性、保温性、クッション性が不十分である。また、比較例2では、発泡性マイクロカプセル粒子を発泡させていない乾燥シートの厚さが1.5mmと、1mmを超えると、リールでの巻き取りで皺や折れが発生し、発泡ムラも発生し、深絞り適性が劣り成形性に問題が出る。さらに、比較例3では、表裏層の熱可塑性合成繊維の割合を50%と増やし、木材パルプの配合率が51%を下回ると熱成形時に金型にくっつき、外れにくくなり、成形性も不良となる。 Specifically, when the blending ratio of the foaming agent in the middle layer of Comparative Example 1 is 9%, the thickness after foaming is 3.2 mm (3.2 times), the amount of foaming is small, and the density is 0.156 g / cm 3 . Since it is high, heat insulating properties, heat retaining properties and cushioning properties are insufficient. Further, in Comparative Example 2, when the thickness of the dry sheet not foamed with the foamable microcapsule particles exceeds 1.5 mm and 1 mm, wrinkles and folds are generated by winding on the reel, and foaming unevenness is also generated. However, the suitability for deep drawing is inferior and there is a problem in moldability. Furthermore, in Comparative Example 3, the ratio of the thermoplastic synthetic fibers in the front and back layers was increased to 50%, and when the blending ratio of the wood pulp was less than 51%, it stuck to the mold at the time of thermoforming, it was difficult to come off, and the moldability was poor. Become.

以上のように、本発明の成形性紙は、木材パルプと熱可塑性合成繊維と発泡性マイクロカプセル粒子とを主体として、構成することによって、深絞りの成形を行うときに混抄紙の破断・皺の発生のない深絞り成形可能であり、成形物の形状安定性もあり、断熱性、保温性、クッション性などの特性をもち、良好な成形性を備え、廃棄する際にも木材繊維成分を51質量%以上としたことによって、容器包装リサイクル法で紙と取り扱える嵩高成形紙を得ることを見出した。   As described above, the formable paper of the present invention is mainly composed of wood pulp, thermoplastic synthetic fibers, and expandable microcapsule particles, so that when the deep drawing is formed, Can be deep-drawn without generation, has shape stability of the molded product, has heat insulation, heat retention, cushioning properties, etc. It has been found that by setting the content to 51% by mass or more, a bulky formed paper that can be handled as paper by the container packaging recycling method is obtained.

Claims (4)

N−BKP(針葉樹晒しクラフトパルプ)、熱可塑性合成繊維及び発泡性マイクロカプセル粒子を主体として組成される熱成形可能な発泡性成形性紙において、該成形性紙が表層、少なくとも1層の中層、裏層で構成される木材パルプ配合率51%以上の多層抄き紙であり、該中層に繊維層100質量%当たり、加熱によってその直径が約4〜5倍及び体積が60倍以上に膨張する発泡性マイクロカプセル粒子を10〜40質量%配合し、表層および裏層に該発泡性マイクロカプセル粒子を配合しないかまたは中層よりも少なく最大10質量%配合し、抄紙機の乾燥工程で、該発泡性マイクロカプセル粒子を発泡させずに乾燥後、キャレンダーに掛け、厚さ1mm以下で巻き取ることを特徴とする深絞り成形性紙。 Thermoformable foamable formable paper composed mainly of N-BKP (softwood bleached kraft pulp), thermoplastic synthetic fiber and foamable microcapsule particles, wherein the formable paper is a surface layer, at least one middle layer, It is a multi-layered paper with a wood pulp content of 51% or more composed of a back layer, and its diameter expands to about 4 to 5 times and its volume to 60 times or more by heating per 100% by mass of the fiber layer. The foamable microcapsule particles are blended in an amount of 10 to 40% by mass, and the foamable microcapsule particles are not blended in the surface layer and the back layer, or are blended in a maximum of 10% by mass less than the middle layer. A deep-drawn formable paper, characterized in that the dry microcapsule particles are dried without being foamed, then applied to a calendar and wound up to a thickness of 1 mm or less. 前記成形性紙の表裏層に前記発泡性マイクロカプセル粒子を繊維層100質量%当たり1〜10質量%添加し、前記多層抄き紙全体としての繊維層100質量%当たり、該発泡性マイクロカプセル粒子が9〜35質量%になることを特徴とする請求項1記載の深絞り成形性紙。   The foamable microcapsule particles are added to the front and back layers of the formable paper in an amount of 1 to 10% by weight per 100% by weight of the fiber layer, and the foamable microcapsule particles per 100% by weight of the fiber layer as the whole multilayer paper. The deep-drawn formable paper according to claim 1, wherein the amount is 9 to 35% by mass. 前記熱可塑性合成繊維が、融点100〜180℃である多分岐状ポリエチレン系合成パルプであることを特徴とする請求項1又は2記載の深絞り成形性紙。   The deep-drawn formable paper according to claim 1 or 2, wherein the thermoplastic synthetic fiber is a multi-branched polyethylene synthetic pulp having a melting point of 100 to 180 ° C. 前記成形性紙において、100〜220℃の熱プレスによって、加熱させ発泡させることを特徴とする請求項1、2又は3記載の深絞り成形性紙。   The deep-drawn formable paper according to claim 1, 2 or 3, wherein the formable paper is heated and foamed by hot pressing at 100 to 220 ° C.
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