JP3351075B2 - Food container manufacturing method - Google Patents

Food container manufacturing method

Info

Publication number
JP3351075B2
JP3351075B2 JP32556793A JP32556793A JP3351075B2 JP 3351075 B2 JP3351075 B2 JP 3351075B2 JP 32556793 A JP32556793 A JP 32556793A JP 32556793 A JP32556793 A JP 32556793A JP 3351075 B2 JP3351075 B2 JP 3351075B2
Authority
JP
Japan
Prior art keywords
container
paper
food container
heat
pulp
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Fee Related
Application number
JP32556793A
Other languages
Japanese (ja)
Other versions
JPH07179643A (en
Inventor
広美 上原口
恒久 重谷
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
New Oji Paper Co Ltd
Oji Holdings Corp
Original Assignee
Oji Holdings Corp
Oji Paper Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Oji Holdings Corp, Oji Paper Co Ltd filed Critical Oji Holdings Corp
Priority to JP32556793A priority Critical patent/JP3351075B2/en
Publication of JPH07179643A publication Critical patent/JPH07179643A/en
Application granted granted Critical
Publication of JP3351075B2 publication Critical patent/JP3351075B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Classifications

    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02ATECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
    • Y02A40/00Adaptation technologies in agriculture, forestry, livestock or agroalimentary production
    • Y02A40/90Adaptation technologies in agriculture, forestry, livestock or agroalimentary production in food processing or handling, e.g. food conservation
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02WCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W90/00Enabling technologies or technologies with a potential or indirect contribution to greenhouse gas [GHG] emissions mitigation
    • Y02W90/10Bio-packaging, e.g. packing containers made from renewable resources or bio-plastics

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【産業上の利用分野】本発明は、食品容器の製造方法に
関するものである。さらに詳しくは、本発明は、高い保
温性、断熱性を要求されるカップ状、トレー状の食品容
器、また青果の包装用紙等クッション性を要求されるト
レー状の容器に利用される食品容器の製造方法に関する
ものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for manufacturing a food container. More specifically, the present invention relates to a food container used as a cup-shaped or tray-shaped food container required to have high heat retention and heat insulation properties, and a tray-shaped container required to have a cushioning property such as wrapping paper for fruits and vegetables. It relates to a manufacturing method.

【0002】[0002]

【従来の技術】従来より食品容器には、発泡ポリスチレ
ン製の容器が断熱性、保温性に優れ、形成、加工性もよ
く更に安価なために多く利用されているが、最近になり
資源、環境保護への関心が急速に高まり、焼却処理が容
易であり、リサイクルが可能であり、更に土壌中の微生
物による生分解が可能である紙を主体とする食品容器へ
の要望が高まってきている。
2. Description of the Related Art Conventionally, foamed polystyrene containers have been widely used as food containers because they are excellent in heat insulation and heat retention, are good in forming and processing, and are inexpensive. Interest in protection is rapidly increasing, and there is an increasing demand for paper-based food containers that are easily incinerated, recyclable, and biodegradable by microorganisms in soil.

【0003】紙基材を主体とするこの種の断熱性、保温
性のある容器としては、内容物の熱が容器を持つ指に直
接伝わらないようにすると共に、容器の強度を向上させ
るために、容器の胴部の外面に多数のリブを付設する方
法が特開昭51ー2576に開示されている。この方法
では、確かにリブの凸面の温度は低く保たれ、容器を持
つ指に熱が伝わらずに持ちやすいものの、リブの凸部分
からの放熱が大きいため内容物の温度低下が速く、容器
の保温性が劣るものであった。また、リブ付容器は断熱
性は優れているものの、見栄え、印刷性が劣るものであ
った。
[0003] Such a heat-insulating and heat-insulating container mainly composed of a paper substrate is intended to prevent the heat of the contents from being directly transmitted to the finger holding the container and to improve the strength of the container. A method of providing a large number of ribs on the outer surface of the body of a container is disclosed in JP-A-51-2576. In this method, the temperature of the convex surface of the rib is certainly kept low, and heat is not transmitted to the finger holding the container, so it is easy to hold the container. The heat retention was inferior. Moreover, the ribbed container was excellent in heat insulation, but was inferior in appearance and printability.

【0004】これらの容器に代わるものとして、加熱に
より発泡する微細粒子状の物質(以下、発泡性粒子と云
う)を混抄して発泡させた密度0.1〜0.4g/cm
3 の紙基材から成る容器が提案されている。このような
密度を有する紙基材からなる容器は、断熱性、クッショ
ン性に優れ、軽量であるため作業性が良く、さらに表面
が平らであるため印刷適正も良いものである。しかしな
がら、このような密度を有する紙基材を用いた場合に
は、成型時に折り曲げた部分に皺が入り易い、あるいは
ヒビ割れを生じ易い等のために製品歩留りが悪く、また
成型性も悪いという欠点を有するものであり、その改善
が必要であった。
[0004] As an alternative to these containers, a density of 0.1 to 0.4 g / cm is obtained by mixing and foaming a particulate material (hereinafter referred to as "expandable particles") which expands by heating.
Containers consisting of three paper substrates have been proposed. A container made of a paper base material having such a density has excellent heat insulating properties and cushioning properties, is light in weight, has good workability, and has a flat surface, and thus has good printability. However, when a paper base material having such a density is used, wrinkles tend to be formed in a bent portion during molding, or cracks easily occur, resulting in poor product yield and poor moldability. It has disadvantages and needs to be improved.

【0005】[0005]

【発明が解決しようとする課題】本発明は、前述の、従
来の0.1〜0.4g/cm3 の密度を有する、発泡性
粒子を発泡させた紙基体からなる食品容器の有する問題
点を克服し、成型時に容器に皺やヒビ割れを生じること
のない製品歩留りの良い食品容器の製造方法を提供する
ものである。
[0008] The present invention, described above, having a density of conventional 0.1 to 0.4 g / cm 3, problems of the food container made of paper substrate obtained by foaming a foamable particles It is intended to provide a method of manufacturing a food container having a good product yield without causing wrinkles or cracks in the container at the time of molding.

【0006】[0006]

【課題を解決するための手段】本発明者等は、発泡性粒
子を含有する紙基体を用いて食品容器を製造する方法を
検討した結果、発泡性粒子を混抄した未発泡のシートを
まず製造しておき、成型時に再含水した後、熱プレスに
より加熱、発泡させ成型する方法により、シートの両面
より熱が伝わるため良好な発泡度を持ち、断熱性、保温
性に優れ、成型時に発泡させるため、皺も傷もない食品
容器を製造できることを見出し、本発明を完成した。
Means for Solving the Problems The present inventors have studied a method of manufacturing a food container using a paper substrate containing expandable particles, and as a result, first produced an unfoamed sheet mixed with expandable particles. In addition, after re-hydrating at the time of molding, it is heated and foamed by hot press, foamed and molded, so that heat is transmitted from both sides of the sheet, it has a good degree of foaming, it has excellent heat insulation and heat retention, and it foams at the time of molding Therefore, they found that a food container without wrinkles and scratches could be manufactured, and completed the present invention.

【0007】すなわち本発明の食品容器の製造方法は、
加熱により発泡する微細粒子を含有する紙基材を、水分
量30〜70%に調整し、次いで熱プレス機により温度
110〜250℃、プレス圧0.05〜1.0kgf/
cm2 の条件で成型を行い、密度0.1〜0.4g/c
3 容器を製造することを特徴とするものである。
That is, the method for producing a food container of the present invention comprises:
The paper base containing the fine particles that expands by heating is adjusted to a water content of 30 to 70%, and then heated to 110 to 250 ° C. under a press pressure of 0.05 to 1.0 kgf /
The molding is performed under the condition of cm 2 and the density is 0.1 to 0.4 g / c.
It is characterized in that to produce the m 3 container.

【0008】以下、本発明の方法について詳しく説明す
る。本発明に使用される紙基材は、通常の製紙で使用さ
れるパルプからなるものが使用可能である。例えば針葉
樹や広葉樹の化学パルプ、機械パルプ等の木材パルプ、
故紙パルプ、さらに、麻、綿等の非木材天然パルプ、ポ
リエチレン、ポリプロピレン等を原料とした合成パルプ
等を挙げることができ、これらを適宜組み合わして使用
する。上記のパルプの他にアクリル繊維、レーヨン繊
維、フェノール樹脂繊維、ポリアミド繊維、ポリエステ
ル繊維等の有機繊維、またガラス繊維、炭素繊維、アル
ミナ繊維等の無機繊維等の各種の繊維を混抄することも
可能である。しかしながら、紙基材の抄紙性、さらに廃
棄の際の燃焼性等を考慮すると、繊維全重量中に木材パ
ルプを70%以上配合していることが望ましい。
Hereinafter, the method of the present invention will be described in detail. As the paper base material used in the present invention, those made of pulp used in ordinary papermaking can be used. For example, wood pulp such as coniferous or hardwood chemical pulp, mechanical pulp, etc.
Waste paper pulp, non-wood natural pulp such as hemp, cotton and the like, synthetic pulp using polyethylene, polypropylene and the like as a raw material, and the like can be used in appropriate combination. In addition to the above pulp, various fibers such as organic fibers such as acrylic fiber, rayon fiber, phenol resin fiber, polyamide fiber and polyester fiber, and inorganic fibers such as glass fiber, carbon fiber and alumina fiber can be mixed. It is. However, considering the papermaking properties of the paper substrate and the flammability at the time of disposal, it is preferable to mix 70% or more of wood pulp with respect to the total weight of the fibers.

【0009】本発明に使用する発泡性粒子は、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
プセルである。このカプセルは、80〜200℃の比較
的低温度で短時間の加熱により、直径が約4〜5倍、体
積が50〜100倍に膨張する平均粒子径5〜30μm
の粒子である。これら発泡性粒子としては、マツモトマ
イクロスフェアーF−3OD、同F−30GS、同F−
20D、同F−50D、同F−80D(以上、松本油脂
製薬(株)製、)、エクスパンセルWU、同DU(以
上、エクスパンセル社(スウェーデン)製、販売元日本
フィライト)が知られているが、もちろんこれらに限定
されるものではない。発泡性粒子の配合量は、パルプ繊
維に対して1〜40%が好ましく、より好ましくは3〜
20%である。配合量が1%未満では発泡性が不十分で
あり、40%を越えて多く配合すると経済性の面で適当
ではない。
[0009] The expandable particles used in the present invention are heat-expandable microcapsules in which a low boiling point solvent is encapsulated in microcapsules. This capsule has an average particle diameter of 5 to 30 μm which expands about 4 to 5 times in diameter and 50 to 100 times in volume by heating for a short time at a relatively low temperature of 80 to 200 ° C.
Particles. These effervescent particles include Matsumoto Microsphere F-3OD, F-30GS, and F-GS.
20D, F-50D, F-80D (Matsumoto Yushi Seiyaku Co., Ltd.), Expancel WU, and Expancel DU (Expensel (Sweden), Nippon Philite) However, the present invention is not limited to these. The blending amount of the expandable particles is preferably 1 to 40%, more preferably 3 to 40% based on the pulp fiber.
20%. If the amount is less than 1%, the foamability is insufficient, and if it exceeds 40%, it is not economically suitable.

【0010】本発明において、紙基材には他に従来より
使用されている各種のアニオン性、ノニオン性、カチオ
ン性あるいは両性の歩留り向上剤、紙力増強剤、サイズ
剤等が適宜選択して使用される。
In the present invention, various anionic, nonionic, cationic or amphoteric retention improvers, paper strength enhancers, sizing agents, etc., which are conventionally used, are appropriately selected for the paper base material. used.

【0011】具体的には、紙力増強剤、歩留り向上剤と
しては、カチオン性、ノニオン性、アニオン性および両
性のポリアクリルアミド樹脂、ポリエチレンイミンおよ
びその誘導体、ポリエチレンオキサイド、ポリアミン、
ポリアミド、ポリアミドポリアミンおよびその誘導体、
カチオン性および両性澱粉、酸化澱粉、カボキシメチル
化澱粉、植物ガム、ポリビニルアルコール、尿素ホルマ
リン樹脂、メラミンホルマリン樹脂、親水性のポリマー
粒子等の有機系化合物、および硫酸バンド、アルミナゾ
ル、塩基性硫酸アルミニウム、塩基性塩化アルミニウ
ム、塩基性ポリ水酸化アルミニウム等のアルミ化合物、
さらに硫酸第一鉄、塩化第二鉄あるいはコロイダルシリ
カ、ベントナイト等の無機系化合物等を適宜組み合わせ
て使用することができる。
Specifically, examples of the paper strength enhancer and the retention aid include cationic, nonionic, anionic and amphoteric polyacrylamide resins, polyethyleneimine and its derivatives, polyethylene oxide, polyamine,
Polyamide, polyamide polyamine and derivatives thereof,
Organic compounds such as cationic and amphoteric starch, oxidized starch, carboxymethylated starch, plant gum, polyvinyl alcohol, urea formalin resin, melamine formalin resin, hydrophilic polymer particles, and sulfate band, alumina sol, basic aluminum sulfate, base Aluminum compounds such as basic aluminum chloride and basic polyaluminum hydroxide,
Further, ferrous sulfate, ferric chloride, or an inorganic compound such as colloidal silica or bentonite can be used in appropriate combination.

【0012】サイズ剤としては、酸性抄紙用サイズ剤と
してロジン系サイズ剤、石油樹脂系サイズ剤、中性抄紙
用サイズ剤としアルキルケテンダイマー系サイズ剤、ア
ルケニル無水コハク酸系サイズ剤等の各種サイズ剤を挙
げることができる。
As the sizing agent, various sizes such as a rosin sizing agent, a petroleum resin sizing agent as an acidic paper sizing agent, an alkyl ketene dimer sizing agent, and an alkenyl succinic anhydride sizing agent as a neutral paper sizing agent. Agents can be mentioned.

【0013】本発明の紙基体にはまた、一般に抄紙で用
いられている填料、例えばタルク、カオリン、焼成カオ
リン、クレー、ケイソウ土、重質炭酸カルシウム、炭酸
マグネシウム、水酸化アルミニウム、二酸化チタン、硫
酸マグネシウム、シリカ、アルミノ珪酸塩、ベントナイ
ト等の鉱物質填料やポリスチレン粒子、尿素ホルマリン
樹脂粒子等の有機合成填料等も適宜選択して使用するこ
とができる。
The paper substrate of the present invention may also contain fillers generally used in papermaking, such as talc, kaolin, calcined kaolin, clay, diatomaceous earth, heavy calcium carbonate, magnesium carbonate, aluminum hydroxide, titanium dioxide, sulfuric acid. Mineral fillers such as magnesium, silica, aluminosilicate and bentonite, and organic synthetic fillers such as polystyrene particles and urea formalin resin particles can also be appropriately selected and used.

【0014】さらに、染料、PH調整剤、スライムコン
トロール剤、消泡剤、粘剤等の各種抄紙用添加助剤も用
途に応じて適宜使用できる。また、サイズプレス、ゲー
トロール等の塗工方法により紙基体の表面に澱粉、ポリ
ビニルアルコール等の水溶性高分子物質、各種表面サイ
ズ剤、顔料等を塗布することも可能である。
Further, various papermaking aids such as dyes, pH adjusters, slime control agents, defoamers, and tackifiers can be used as appropriate according to the intended use. It is also possible to apply starch, water-soluble polymer substances such as polyvinyl alcohol, various surface sizing agents, pigments and the like to the surface of the paper substrate by a coating method such as a size press or a gate roll.

【0015】上記の原料を用いて、通常の抄紙マシーン
により抄紙を行い、紙基体を製造する。まず、抄紙工程
のワイヤーパートを経てシート状とした後、プレスパー
トにより脱水し、ドライヤーパートにより乾燥処理をす
る。この時のドライヤー温度は、発泡性粒子の発泡開始
温度以下にする必要があり、具体的には70〜100
℃、好ましくは極力発泡を抑えるために70〜85℃付
近が適当である。得られた原紙は、水分量2〜50%で
巻き取りにする。
Using the above-mentioned raw materials, papermaking is carried out by an ordinary papermaking machine to produce a paper substrate. First, after a sheet is formed through a wire part in a paper making process, dehydration is performed by a press part and drying treatment is performed by a dryer part. The dryer temperature at this time needs to be equal to or lower than the foaming start temperature of the foamable particles.
C., preferably around 70 to 85 C. to minimize foaming. The obtained base paper is wound up at a water content of 2 to 50%.

【0016】次いで、得られた紙基材を用いて、食品容
器を製造する。この際、紙基材の水分が少ない場合は、
再び含水してシートの熱伝達をよくした後、熱プレス機
で成形する。このときの水分量としては30〜70%が
好ましい。紙基材の水分量が30%未満では発泡が充分
でなく不都合であり、また、70%を越えて多くなる
と、プレス成形時に水蒸気圧で紙基材が破裂し、良好な
成形品が得られないことがある。
Next, a food container is manufactured using the obtained paper base material. At this time, if the water content of the paper substrate is low,
After the sheet is again hydrated to improve the heat transfer of the sheet, it is formed by a hot press. The water content at this time is preferably 30 to 70%. If the water content of the paper base is less than 30%, foaming is not sufficient, which is inconvenient. If it exceeds 70%, the paper base bursts due to steam pressure during press molding, and a good molded product is obtained. There may not be.

【0017】また、熱プレス時の温度としては、発泡剤
が充分に発泡するのに必要な110〜250℃が好まし
い。さらに圧力は、プレス上昇圧を除いて、成形単位面
積あたり0.05〜1.0kgf/cm2 の範囲が適当
である。プレス圧が0.05kgf/cm2 未満では、
熱がシートに充分に伝わらず、発泡が不十分になつこと
があり、また1.0kgf/cm2 を越えて高くなる
と、発泡性粒子の膨張圧力を上回る為に発泡した粒子が
つぶされて密度が高くなる。
The temperature at the time of hot pressing is preferably 110 to 250 ° C. necessary for the foaming agent to foam sufficiently. Further, the pressure is suitably in the range of 0.05 to 1.0 kgf / cm 2 per molding unit area, excluding the pressurizing pressure. If the press pressure is less than 0.05 kgf / cm 2 ,
When the heat is not sufficiently transmitted to the sheet, the foaming may be insufficient. When the heat exceeds 1.0 kgf / cm 2 , the expanded particles are crushed to exceed the expansion pressure of the expandable particles, and the density is increased. Will be higher.

【0018】成型装置には、電動加圧・蒸気加圧・オイ
ル加圧等のプレス成型機があり、一面取りが好ましい。
加圧の初期はやや高圧でも、のちに低圧になるものなら
ばいずれも用いることができる。加圧時間は温度により
異なるが、通常5〜60秒である。加圧時の温度が15
0℃以上の場合、長時間加圧すると過度に乾燥したり、
焦げたりすることがあるため、短時間で成型する必要が
ある。成型後、必要があれば、送風乾燥機等で成型品を
完全に乾燥することもできる。
The molding apparatus includes a press molding machine for electric pressurization, steam pressurization, oil pressurization, and the like, and a single chamfer is preferable.
Any pressure may be used in the initial stage of pressurization, even if the pressure is slightly high, but the pressure will be low at a later time. The pressurization time varies depending on the temperature, but is usually 5 to 60 seconds. Temperature at pressurization is 15
If the temperature is 0 ° C or higher, it will dry excessively when pressed for a long time,
It is necessary to mold in a short time because it may burn. After the molding, if necessary, the molded article can be completely dried by a blow dryer or the like.

【0019】本発明において、発泡性粒子を含有する紙
基材の坪量は25〜400g/m2であることが好まし
く、より好ましくは50〜300g/m2 である。坪量
が25g/m2 未満では、十分な断熱性がある食品容器
が得られず、また、400g/m2 を越えると抄紙機の
乾燥工程のドライヤーの負荷が大きくなり、紙基材の乾
燥が不十分になる。
[0019] In the present invention, the basis weight of the paper base material containing expandable particles is preferably from 25~400g / m 2, more preferably from 50 to 300 g / m 2. If the grammage is less than 25 g / m 2 , a food container having sufficient heat insulating properties cannot be obtained. If the grammage exceeds 400 g / m 2 , the load of the dryer in the drying step of the paper machine increases, and the drying of the paper base material Becomes insufficient.

【0020】本発明の密度0.1〜0.4g/cm3
容器の坪量は、ファーストフードや中華饅頭に使われる
低温用容器には25〜150g/m2 が好ましく、一方
ラーメンカップ等に使用される高温用容器は、坪量10
0〜300g/m2 のものを用いることが好ましい。例
えば、3分後の容器外層の表面温度が75℃以下であれ
ば、高温用容器としては適当である。このように、適宜
必要に応じて密度と坪量を選んで調整することができ
る。さらに、本発明の容器は、青果用のクッション性ト
レー、精肉用トレー等各種のトレーとしても使用でき
る。
The basis weight of the container of the present invention having a density of 0.1 to 0.4 g / cm 3 is preferably 25 to 150 g / m 2 for a low-temperature container used for fast food or Chinese steamed bun, while a ramen cup or the like is used. High temperature container used for
It is preferable to use one having 0 to 300 g / m 2 . For example, if the surface temperature of the outer layer of the container after 3 minutes is 75 ° C. or less, it is suitable as a high-temperature container. As described above, the density and the basis weight can be appropriately selected and adjusted as needed. Further, the container of the present invention can be used as various trays such as a cushioning tray for fruits and vegetables, a tray for meat, and the like.

【0021】本発明の食品容器は、加圧成型後さらに必
要に応じて、ポリエチレン樹脂等によるラミネート処理
やパラフィンワックス等による撥水処理を施して、耐水
加工処理を施してもよい。本発明の食品容器の形状は特
に限定されるものではなく、中に収納する食品の形状に
合わせて適宜成型、加工すればよい。
The food container of the present invention may be subjected to a water-resistant treatment after the pressure molding, if necessary, by a lamination treatment with a polyethylene resin or the like or a water-repellent treatment with a paraffin wax or the like. The shape of the food container of the present invention is not particularly limited, and may be appropriately molded and processed according to the shape of the food stored therein.

【0022】[0022]

【実施例】以下、実施例により本発明をさらに詳細に説
明するが、もちろん本発明はこれらの実施例によって限
定されるものではない。なお、実施例中の「%」はすべ
て「重量%」を示す。
EXAMPLES The present invention will be described in more detail with reference to the following Examples, which, of course, are not intended to limit the present invention. In addition, all "%" in an Example shows "weight%."

【0023】実施例1 カナダ標準濾水度450mlに叩解した広葉樹晒パルプ
(LBKP)80%とカナダ標準濾水度470mlに叩
解した針葉樹晒パルプ(NBKP)20%とからなるパ
ルプを分散したパルプスラリーに、パルプ絶乾重量に対
して発泡性マイクロカプセル粒子(松本油脂製薬(株)
製、マツモトマイクロスフェアーF−30D、粒子径10
〜20μm)を10%、乾燥紙力増強剤(荒川化学工業
(株)製、ポリストロン−117)を0.2%、カチオ
ン化澱粉(王子ナショナル社製、CATO−15)を
1.0%、アルキルケテンダイマー系サイズ剤(荒川化
学工業(株)製、サイズスパンK903)を0.03
%、湿潤紙力増強剤(DICハーキュレス社製、カイメ
ン−557H)を0.4%添加し、パルプ濃度0.03
%、PH7.3に調整し、インレット原料とした。得ら
れたインレット原料を用いて円網抄紙機により抄紙し、
70〜75℃の多筒ドライヤーで水分10%に乾燥し、
坪量151g/m2 、密度0.55g/cm3 の紙基材
を得た。その後オフラインで、平底のトレーにより、紙
基材の水分量を55%に調整し、次いで、温度150
℃、成形単位面積あたりの圧力0.1kgfの条件下
で、熱プレス機により成型・発泡させ、縦15cm×横
9.0cm×深さ1.5cmの平型トレーに成形した
後、送風乾燥機にて乾燥し食品容器を作製した。
Example 1 Pulp slurry in which pulp composed of 80% hardwood bleached pulp (LBKP) beaten to a Canadian standard freeness of 450 ml and 20% softwood bleached pulp (NBKP) beaten to a Canadian standard freeness of 470 ml was dispersed. In addition, effervescent microcapsule particles (Matsumoto Yushi Pharmaceutical Co., Ltd.)
Manufactured by Matsumoto Microsphere F-30D, particle size 10
10%, dry paper strength agent (Polystron-117, manufactured by Arakawa Chemical Industries, Ltd.) 0.2%, and cationized starch (CATO-15, manufactured by Oji National Co., Ltd.) 1.0%. , An alkyl ketene dimer-based sizing agent (size span K903, manufactured by Arakawa Chemical Industries, Ltd.)
%, 0.4% wet paper strength enhancer (manufactured by DIC Hercules, Kaimen-557H) was added, and the pulp concentration was 0.03%.
%, PH was adjusted to 7.3 to obtain an inlet raw material. Using the obtained inlet raw material, papermaking is performed using a circular paper machine,
Dry to 10% moisture with a multi-cylinder dryer at 70-75 ° C,
A paper base material having a basis weight of 151 g / m 2 and a density of 0.55 g / cm 3 was obtained. Then, off-line, the water content of the paper substrate was adjusted to 55% with a flat bottom tray,
Under a condition of 0 ° C. and a pressure of 0.1 kgf per unit area of molding, the mixture is molded and foamed by a hot press machine, formed into a flat tray of 15 cm long × 9.0 cm × 1.5 cm deep, and then blow-dried. To produce a food container.

【0024】実施例2 紙基材として坪量が320g/m2 、密度が0.54g
/cm3 のものを使用した以外は、実施例1と同様の手
順で食品容器を作製した。
Example 2 A paper base material having a basis weight of 320 g / m 2 and a density of 0.54 g
Except for using those / cm 3 was prepared food containers in the same manner as in Example 1.

【0025】実施例3 オフラインでの紙基材の含水量を65%にした以外は、
実施例1と同様の条件下で食品容器を作製した。
Example 3 Except that the water content of the paper base material offline was 65%.
A food container was produced under the same conditions as in Example 1.

【0026】実施例4 熱プレス機の温度を200℃にした以外は、実施例1と
同様の条件下で食品容器を作製した。
Example 4 A food container was prepared under the same conditions as in Example 1 except that the temperature of the hot press was set to 200 ° C.

【0027】実施例5 熱プレス機のプレス圧を0.08kgf/cm2 にした
以外は、実施例1と同様の条件下で食品容器を作製し
た。
Example 5 A food container was produced under the same conditions as in Example 1 except that the pressing pressure of the hot press was changed to 0.08 kgf / cm 2 .

【0028】実施例6 熱プレス機のプレス圧を0.4kgf/cm2 にした以
外は、実施例1と同様の条件下で食品容器を作製した。
Example 6 A food container was produced under the same conditions as in Example 1 except that the pressure of the hot press was changed to 0.4 kgf / cm 2 .

【0029】実施例7 熱プレス機のプレス温度を200℃、プレス圧を0.7
2kgf/cm2 にした以外は、実施例1と同様の条件
下で食品容器を作製した。
Example 7 The press temperature of the hot press was 200 ° C. and the press pressure was 0.7.
A food container was prepared under the same conditions as in Example 1 except that the weight was changed to 2 kgf / cm 2 .

【0030】比較例1 オフラインでの紙基材の含水量を20%にした以外は、
実施例1と同様の条件下で食品容器を作製した。
Comparative Example 1 Except that the water content of the paper base material off-line was 20%
A food container was produced under the same conditions as in Example 1.

【0031】比較例2 オフラインでの紙基材の含水量を72%にした以外は、
実施例1と同様の条件下で食品容器を作製した。
COMPARATIVE EXAMPLE 2 Except that the water content of the paper base material off-line was changed to 72%,
A food container was produced under the same conditions as in Example 1.

【0032】比較例3 熱プレス機のプレス圧を1.3kgf/cm2 にした以
外は、実施例1と同様の条件下で食品容器を作製した。
Comparative Example 3 A food container was produced under the same conditions as in Example 1 except that the pressing pressure of the hot press was 1.3 kgf / cm 2 .

【0033】実施例1〜4及び比較例1〜3で得られた
食品容器の厚さ及び密度を測定し、さらに成型性、断熱
性を評価した。結果を表1に示す。なお、成形性につい
ては、容器の折り曲げ部の皺の有無で評価した。また、
断熱性の評価は、以下の要領で熱拡散率を測定して熱伝
導率を算出して行った。熱伝導率の値が7.0×10-2
w/m/k以下であれば断熱性は実用的な水準にある。 測定法:レーザーフラッシュ法により熱拡散率を測定
し、下記の式により熱伝導率(λ)を算出した。なお、
測定は、理学電気社製のLF/TCM(FA8510B
型)測定機を用いて行った。 λ=α・Cp・ρ λ;熱伝導率(w/m/k) α;熱拡散率(cm2 /sec) Cp;熱容量(J/g・℃)、紙の場合は1.34で計
算 ρ;密度(g/cm3
The thickness and density of the food containers obtained in Examples 1 to 4 and Comparative Examples 1 to 3 were measured, and the moldability and heat insulation were evaluated. Table 1 shows the results. In addition, about the moldability, it evaluated by the presence or absence of the wrinkle of the bending part of a container. Also,
The heat insulation was evaluated by measuring the thermal diffusivity and calculating the thermal conductivity in the following manner. The value of thermal conductivity is 7.0 × 10 -2
If it is less than w / m / k, the heat insulating property is at a practical level. Measurement method: The thermal diffusivity was measured by a laser flash method, and the thermal conductivity (λ) was calculated by the following equation. In addition,
The measurement was performed using LF / TCM (FA8510B manufactured by Rigaku Denki).
Type) The measurement was performed using a measuring machine. λ = α · Cp · ρ λ; Thermal conductivity (w / m / k) α; Thermal diffusivity (cm 2 / sec) Cp: Heat capacity (J / g · ° C.), calculated with 1.34 for paper ρ; density (g / cm 3 )

【0034】[0034]

【表1】 [Table 1]

【0035】表1から明らかなように、実施例1〜4の
本発明の紙基材からは、熱プレス発泡により、良好な発
泡性を有する食品容器が作製された。また、得られた食
品容器は成形性が良く、断熱性も良好である。
As is clear from Table 1, food containers having good foaming properties were produced from the paper substrates of the present invention of Examples 1 to 4 by hot press foaming. Moreover, the obtained food container has good moldability and good heat insulation.

【0036】[0036]

【発明の効果】本発明の方法で作製された食品容器は、
発泡性粒子による多数の独立気泡のため、断熱性、保温
性が良く、さらに軽量で成形性に富むものであり、紙製
の容器としては画期的なものが得られ、また見栄えも良
く、実用上極めて有用なものである。
The food container produced by the method of the present invention comprises:
Because of the large number of closed cells made of expandable particles, it has good heat insulation and heat retention properties, is lightweight and has good moldability, and as a paper container, an epoch-making thing is obtained, and it has good appearance, It is extremely useful in practice.

Claims (1)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】 加熱により発泡する微細粒子を含有する
紙基材を、水分量を30〜70%に調整し、次いで熱プ
レス機により温度110〜250℃、プレス圧0.05
〜1.0kgf/cm2 の条件で成型を行い、密度0.
1〜0.4g/cm3 容器を製造することを特徴とする
食品容器の製造方法。
1. A paper substrate containing fine particles which expands upon heating is adjusted to a water content of 30 to 70%, and then heated to a temperature of 110 to 250 ° C. under a press pressure of 0.05%.
Molding is performed under the condition of 1.0 to 1.0 kgf / cm 2 , and the density is 0.
A method for producing a food container, comprising producing a 1 to 0.4 g / cm 3 container.
JP32556793A 1993-12-24 1993-12-24 Food container manufacturing method Expired - Fee Related JP3351075B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP32556793A JP3351075B2 (en) 1993-12-24 1993-12-24 Food container manufacturing method

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP32556793A JP3351075B2 (en) 1993-12-24 1993-12-24 Food container manufacturing method

Publications (2)

Publication Number Publication Date
JPH07179643A JPH07179643A (en) 1995-07-18
JP3351075B2 true JP3351075B2 (en) 2002-11-25

Family

ID=18178335

Family Applications (1)

Application Number Title Priority Date Filing Date
JP32556793A Expired - Fee Related JP3351075B2 (en) 1993-12-24 1993-12-24 Food container manufacturing method

Country Status (1)

Country Link
JP (1) JP3351075B2 (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR101307108B1 (en) 2011-05-17 2013-09-11 율촌화학 주식회사 Composition for starch bowl, starch bowl using the same and method for preparing starch bowl using the same

Also Published As

Publication number Publication date
JPH07179643A (en) 1995-07-18

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