JPH0539379A - Moisture conditioning composition and moisture conditioning molded article - Google Patents

Moisture conditioning composition and moisture conditioning molded article

Info

Publication number
JPH0539379A
JPH0539379A JP3222442A JP22244291A JPH0539379A JP H0539379 A JPH0539379 A JP H0539379A JP 3222442 A JP3222442 A JP 3222442A JP 22244291 A JP22244291 A JP 22244291A JP H0539379 A JPH0539379 A JP H0539379A
Authority
JP
Japan
Prior art keywords
humidity
magnesium sulfate
humidity control
molded article
moisture
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.)
Pending
Application number
JP3222442A
Other languages
Japanese (ja)
Inventor
Katsumi Shigeta
勝巳 繁田
Eiji Isojima
英二 礒嶌
Hironaga Hayashi
裕修 林
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.)
SASAKI KAGAKU YAKUHIN KK
TOMITA SEIYAKU KK
Tomita Pharmaceutical Co Ltd
Original Assignee
SASAKI KAGAKU YAKUHIN KK
TOMITA SEIYAKU KK
Tomita Pharmaceutical 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 SASAKI KAGAKU YAKUHIN KK, TOMITA SEIYAKU KK, Tomita Pharmaceutical Co Ltd filed Critical SASAKI KAGAKU YAKUHIN KK
Priority to JP3222442A priority Critical patent/JPH0539379A/en
Priority to TW080108489A priority patent/TW234136B/zh
Priority to KR1019910019245A priority patent/KR940006399B1/en
Publication of JPH0539379A publication Critical patent/JPH0539379A/en
Pending legal-status Critical Current

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D53/00Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
    • B01D53/26Drying gases or vapours
    • B01D53/28Selection of materials for use as drying agents

Abstract

PURPOSE:To provide a moisture conditioning composition and a moisture conditioning molded article which have a moisture conditioning function capable of maintaining humidity constant. CONSTITUTION:The objective moisture conditioning composition prepared by mixing 100 pts.wt. thermoplastic resin with 5-400 pts.wt. magnesium sulfate represented by formula MgSO4.nH2O (wherein 0<=n<=3) and having an average particle size of 30mum or less, and the moisture conditioning molded article such as film prepared from the composition.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は湿度を一定湿度に保持し
得る調湿機能のある調湿性組成物及びこの組成物から得
られる調湿性成形品に関する。
TECHNICAL FIELD The present invention relates to a humidity-controlling composition having a humidity-controlling function capable of keeping humidity at a constant humidity, and a humidity-controlling molded article obtained from the composition.

【0002】[0002]

【従来の技術】従来、食品、医薬品、電子部品、精密機
械等のあらゆる分野において吸湿に起因する酸化等によ
る商品等の品質劣化を防ぐ目的で、シリカゲル、塩化カ
ルシウム、生石灰、ゼオライト等の乾燥剤が使用されて
いる。これらの乾燥剤は、粒状あるいは粉状の状態で、
紙、不織布等によつて包装されるか、もしくは、容器等
に封入された状態で商品とともに包材へ投入されて用い
られている。
2. Description of the Related Art Conventionally, desiccants such as silica gel, calcium chloride, quick lime, zeolite, etc. for the purpose of preventing quality deterioration of products such as foods, pharmaceuticals, electronic parts, precision machinery, etc. due to oxidation due to moisture absorption. Is used. These desiccants are in a granular or powder state,
It is used by being wrapped with paper, non-woven fabric, or the like, or being put in a packaging material together with a product in a state of being enclosed in a container or the like.

【0003】[0003]

【発明が解決しようとする課題】従来より乾燥剤として
使用されているシリカゲル、ゼオライト、塩化カルシウ
ム、生石灰等の乾燥剤はその物理的、化学的性質により
乾燥力や吸湿力が強く、密封した容器及び袋等に入れる
と短期間にその内部の水分を取り、湿度0%になるまで
限りなく内部の水分を取り続ける。これは、それぞれの
乾燥剤が持つ化学的、物理的作用であり、外部に対して
商品を密封するために用いられる包材などに入れて使用
する場合、湿度を一定に保ち内容物に適度な湿度を保持
させることができなかつた。すなわち、従来の乾燥剤は
湿度調節機能はなかつた。
The desiccants such as silica gel, zeolite, calcium chloride and quick lime that have been conventionally used as desiccants have strong drying power and hygroscopicity due to their physical and chemical properties, and are hermetically sealed containers. Also, when placed in a bag or the like, the water inside is taken for a short period of time, and the water inside is taken infinitely until the humidity reaches 0%. This is the chemical and physical action of each desiccant, and when used by putting it in the packaging material used to seal the product from the outside, keep the humidity constant and keep it appropriate for the contents. I couldn't keep the humidity. That is, the conventional desiccant has no humidity control function.

【0004】本発明は、従来の乾燥剤では可能でなかつ
た調湿機能を有し、湿度60〜10%の範囲で任意の一
定湿度に保持することができる調湿機能のある調湿性組
成物及びこの組成物から得られる調湿性成形品を提供す
ることを目的としている。
The present invention has a humidity-controlling composition having a humidity-controlling function which is not possible with a conventional desiccant and having a humidity-controlling function capable of maintaining an arbitrary constant humidity in the range of 60 to 10%. And a humidity-conditioning molded article obtained from this composition.

【0005】[0005]

【課題を解決するための手段】本発明は、上記の目的を
達成するために本発明者らが鋭意研究を重ねた結果完成
したものであつて、熱可塑性樹脂に、特定の調湿剤の特
定量を配合することにより、調湿性を有し、しかも吸湿
力、飛散性、持続力、潮解性においても優れている調湿
性組成物を提供することに成功したものである。
Means for Solving the Problems The present invention has been completed as a result of intensive studies conducted by the present inventors in order to achieve the above object. By blending a specific amount, the present invention succeeded in providing a humidity-controlling composition having a humidity-controlling property and also excellent in hygroscopicity, scattering property, sustainability and deliquescent property.

【0006】すなわち、本発明の調湿性組成物は、熱可
塑性樹脂100重量部に対して、式MgSO4 ・nH2
O(但し0≦n≦3)で表され、かつ平均粒子径が30
μm以下である硫酸マグネシウムを5〜400重量部配
合してなるものである。
That is, the humidity control composition of the present invention has the formula MgSO 4 .nH 2 with respect to 100 parts by weight of the thermoplastic resin.
O (however, 0 ≦ n ≦ 3) and has an average particle size of 30
5 to 400 parts by weight of magnesium sulfate having a size of μm or less is blended.

【0007】このように規定される硫酸マグネシウム
は、湿気を吸収すると、最初に6水塩が生成し、吸湿量
の増加に従い6水塩のみが増え、その間1〜5水塩は生
成せず、無水塩が僅かになった時点、すなわち、吸水率
が43〜48%の時に7水塩に変化する調湿剤である。
When magnesium sulfate defined in this way absorbs moisture, hexahydrate is first formed, and as the amount of absorbed moisture increases, only hexahydrate increases, while 1-5 hydrate does not form, It is a humidity control agent that changes to 7-hydrate when the amount of the anhydrous salt becomes small, that is, when the water absorption is 43 to 48%.

【0008】本発明に使用される熱可塑性樹脂として
は、特に限定されず公知のものを使用できるが、、例え
ばポリエチレン(PE)、ポリプロピレン(PP)、ポ
リカ−ボネ−ト、ポリアミド(PA)、エチレン−酢酸
ビニ−ル共重合体(EVA)、エチレン−メチルアクリ
レ−ト共重合体(EMA)、エチレン−メタアクリレ−
ト共重合体、ポリ塩化ビニル、ポリスチレン、ポリエス
テル、ポリ塩化ビニリデン(PVDC)等が挙げられ、
これらのうちの一種又は二種以上を用いることができ
る。
The thermoplastic resin used in the present invention is not particularly limited, and known ones can be used. For example, polyethylene (PE), polypropylene (PP), polycarbonate, polyamide (PA), Ethylene-vinyl acetate copolymer (EVA), ethylene-methyl acrylate copolymer (EMA), ethylene-methacrylate
Copolymers, polyvinyl chloride, polystyrene, polyester, polyvinylidene chloride (PVDC), and the like,
One or more of these can be used.

【0009】また、本発明において、熱可塑性樹脂とと
もに用いられる調湿剤としては、式MgSO4 ・nH2
O(但し0≦n≦3)で表される硫酸マグネシウム、特
に前記樹脂に対して卓越した分散性を有する硫酸マグネ
シウムが好ましい。3水和物をこえた硫酸マグネシウム
水和物は樹脂とともに混練する時に、混練時の加温によ
つて自己の持つ水和水を放出し、製造中の障害が生じ、
有効な機能を発揮し得る調湿性組成物を得ることができ
ず、また、この組成物からフィルム、シ−ト、容器等の
成形品を作製しようとしても、商品価値のある調湿性成
形品を得ることができない。また、上記の調湿剤は平均
粒子径30μm以下のものである。かかる平均粒子径の
小さい硫酸マグネシウムは、比表面積の変動範囲が最大
で4.0〜1.5m2 /gであつてその変動が小さい。
なお、必要に応じて、硫酸マグネシウムは異なつた粒子
径のものを混練して用いてもよい。
In the present invention, the humidity control agent used together with the thermoplastic resin is represented by the formula MgSO 4 .nH 2
Magnesium sulfate represented by O (where 0 ≦ n ≦ 3), particularly magnesium sulfate having excellent dispersibility in the resin, is preferable. Magnesium sulfate hydrate that exceeds trihydrate, when kneading with resin, releases its own water of hydration due to the heating during kneading, which causes problems during production.
It is not possible to obtain a humidity control composition capable of exerting an effective function, and even if an attempt is made to form a molded article such as a film, a sheet or a container from this composition, a humidity control molded article having commercial value is obtained. Can't get The above-mentioned humidity conditioner has an average particle diameter of 30 μm or less. Such magnesium sulfate having a small average particle diameter has a maximum fluctuation range of the specific surface area of 4.0 to 1.5 m 2 / g, and its fluctuation is small.
If necessary, magnesium sulfate having different particle diameters may be kneaded and used.

【0010】ここに、硫酸マグネシウムの平均粒子径が
30μmを越した場合には、吸湿性組成物の吸湿速度が
遅くなる。また、硫酸マグネシウムの比表面積の変動が
大きくなり、調湿性組成物から成形品を作製した場合、
吸湿に伴い成形品の膨脹、収縮、亀裂が発生し寸法安定
性を保持することができず、実用的な成形品を得ること
ができなくなる。
When the average particle diameter of magnesium sulfate exceeds 30 μm, the moisture absorption rate of the hygroscopic composition becomes slow. Further, when the fluctuation of the specific surface area of magnesium sulfate becomes large, and a molded article is produced from the humidity control composition,
Due to the absorption of moisture, the molded product expands, contracts, and cracks, so that the dimensional stability cannot be maintained and a practical molded product cannot be obtained.

【0011】本発明において、配合する原料の割合は、
熱可塑性樹脂100重量部に対し、調湿剤5〜400重
量部であり、この範囲内において用途に応じて適宜選択
される。調湿剤の割合が上記範囲の場合には、調湿剤の
樹脂中での分散性がよく、高い調湿性、吸湿性、保水
性、持続性を有し、しかも成形適性に優れたものとな
り、本発明の目的とする調湿性組成物を得ることができ
る。
In the present invention, the ratio of the raw materials to be blended is
The humidity control agent is 5 to 400 parts by weight with respect to 100 parts by weight of the thermoplastic resin, and is appropriately selected within this range according to the application. When the proportion of the humidity control agent is in the above range, the dispersibility of the humidity control agent in the resin is good, and the humidity control property, the hygroscopicity, the water retention property and the durability are high, and the moldability is excellent. The humidity control composition intended by the present invention can be obtained.

【0012】本発明の調湿性組成物においては、上記熱
可塑性樹脂及び調湿剤のほかに、発泡剤を原料として添
加することもできる。発泡剤としては、特に限定されず
公知のものを広く使用することができ、例えばアゾイソ
ブチロニトリル、アゾジカルボンアミド、4,4´−オ
キシベンゼンスルホニルヒドラジッド等が挙げられる。
発泡剤の使用量は、熱可塑性樹脂100重量部に対し、
0.2〜10重量部が好ましい。この発泡剤の添加され
た発泡性調湿性組成物から得られる発泡調湿性成形体
は、軽量で、発泡体内部にまで吸湿効果が及ぶために更
に高い吸湿力をもたらすものである。
In the humidity control composition of the present invention, in addition to the thermoplastic resin and the humidity control agent, a foaming agent may be added as a raw material. The foaming agent is not particularly limited and widely known agents can be widely used. Examples thereof include azoisobutyronitrile, azodicarbonamide, and 4,4′-oxybenzenesulfonyl hydrazide.
The amount of the foaming agent used is 100 parts by weight of the thermoplastic resin,
0.2 to 10 parts by weight is preferable. The foamed humidity-controlling molded article obtained from the foaming humidity-controlling composition to which the foaming agent is added is lightweight and has a higher hygroscopic force because the hygroscopic effect extends to the inside of the foamed article.

【0013】このほかに、添加剤として公知の可塑剤、
安定剤、滑剤、着色剤等を必要に応じ、本発明の目的を
阻害しない程度に適宜加えてもよい。
Besides, a plasticizer known as an additive,
Stabilizers, lubricants, coloring agents and the like may be added as needed, as long as they do not impair the object of the present invention.

【0014】また、本発明では本発明の調湿性組成物を
成形することにより得られる調湿性成形品をも包含する
ものである。
The present invention also includes a humidity-controlling molded article obtained by molding the humidity-controlling composition of the present invention.

【0015】本発明の調湿性組成物及びその成形品の製
造方法としては、特に制限はなく、通常次のような方法
で製造することができる。すなわち、前記の熱可塑性樹
脂、調湿剤及び必要によりその他の添加剤を、ミキシン
グロ−ル等の混練機、混練成形機等を用いて約100〜
350℃の温度で約5〜40分間混練すれば調湿性組成
物が得られ、さらに、この組成物を成形することにより
調湿性成形品が得られる。
The method for producing the humidity control composition of the present invention and the molded article thereof is not particularly limited, and it can be usually produced by the following method. That is, about 100 to about 100 parts of the above-mentioned thermoplastic resin, humidity control agent and, if necessary, other additives are mixed using a kneading machine such as mixin-gall or a kneading molding machine.
A humidity-controlling composition can be obtained by kneading at a temperature of 350 ° C. for about 5 to 40 minutes, and a humidity-controlling molded article can be obtained by molding the composition.

【0016】さらに、本発明の調湿性成形品には、調湿
性組成物から得られる調湿性積層材の少なくとも一種を
積層した積層調湿性成形品をも包含するものである。該
調湿性積層材と積層される他の積層材としては、本発明
の組成物の原料である前記の熱可塑性樹脂等の樹脂類、
紙類、繊維類、金属類、各種塗料、各種接着剤等を用い
ることができる。なお、本発明の調湿性組成物から得ら
れる調湿性積層材の少なくとも一種とは、組成の異なる
本発明の調湿性組成物から得られる二種以上の積層材を
も用いることができることを意味する。積層材の種類、
量(厚み)、及び積層数は、本発明の目的を達成する限
り限定されず広範に使用することができ、用途(要求)
に応じ適宜選択される。
Further, the humidity control molded article of the present invention includes a laminated humidity control molded article obtained by laminating at least one of the humidity control laminates obtained from the humidity control composition. Other laminated materials to be laminated with the humidity-controlling laminated material include resins such as the above-mentioned thermoplastic resins which are raw materials of the composition of the present invention,
Papers, fibers, metals, various paints, various adhesives, etc. can be used. Note that at least one of the humidity-controlling laminates obtained from the humidity-controlling composition of the present invention means that two or more kinds of laminates obtained from the humidity-controlling composition of the present invention having different compositions can also be used. .. Type of laminated material,
The amount (thickness) and the number of laminated layers are not limited as long as the object of the present invention is achieved, and can be widely used.
It is selected as appropriate.

【0017】上記積層化の最も一般的な例は、上記調湿
性積層材でラミネ−トされたフィルム、シ−トもしくは
プレ−トである。この積層構成の場合の樹脂構成につい
ての具体例を次に列記するが、本発明はこれに限られる
ことはない。
The most common example of the lamination is a film, sheet or plate laminated with the humidity control laminate. Specific examples of the resin structure in the case of this laminated structure are listed below, but the present invention is not limited to this.

【0018】低密度ポリエチレン(LDPE)/中密度
ポリエチレン(MDPE) 高密度ポリエチレン(HDPE)/LDPE/HDPE HDPE/LDPE/LDPE HDPE/EMA/LDPE HDPE/アイオノマ− PA/アイオノマ− PP/EVA/PP PP/EVA/LDPE PA/接着性PE/アイオノマ− PA/接着性PE/EVA PA/接着性PE/HDPE PA/接着性PE/直鎖状低密度ポリエチレン(LLD
PE) PA/接着性LLDPE/LLDPE PA/接着性PP/PP LDPE/PA/EVA EVA/PVDC/EVA EVA/PVDC/アイオノマ− LDPE/接着性PE/PA なお、上記積層例において、「接着性」とは接着剤によ
る積層を意味する。また調湿剤は上記の樹脂層のいずれ
に含有されてもよいが、積層化の主たる目的が吸湿性包
材の製造にあることから外層に含有させる必要はない。
さらにアルミニウム箔等を貼り合わせて外部からの水
分、光等をほぼ完全に遮断することもできる。積層は、
押出しラミネ−ション法、共押出しラミネ−ション法、
多層射出成形法、接着法等により容易に行うことがで
き、結果として得られる積層体は、更に袋状または容器
状に容易に加工することができる。このように、包材と
して、必要ならば外層に防水性の材質を、内層に水分浸
透性の保護材を積層した本発明の積層調湿性成形品は、
調湿及び吸湿効果、その寿命、耐久性、遮光性、帯電防
止性、安全性、安定性が向上し、品質劣化防止の効果に
より一層優れ、しかも、あらゆる使用環境に対応し得る
より機能的なものである。
Low Density Polyethylene (LDPE) / Medium Density Polyethylene (MDPE) High Density Polyethylene (HDPE) / LDPE / HDPE HDPE / LDPE / LDPE HDPE / EMA / LDPE HDPE / Ionomer PA / Ionomer PP / EVA / PP PP / EVA / LDPE PA / Adhesive PE / Ionomer-PA / Adhesive PE / EVA PA / Adhesive PE / HDPE PA / Adhesive PE / Linear low-density polyethylene (LLD)
PE) PA / adhesive LLDPE / LLDPE PA / adhesive PP / PP LDPE / PA / EVA EVA / PVDC / EVA EVA / PVDC / ionomer-LDPE / adhesive PE / PA In the above lamination example, “adhesiveness” Means laminating with an adhesive. The humidity control agent may be contained in any of the above resin layers, but it is not necessary to contain it in the outer layer since the main purpose of lamination is to produce the hygroscopic packaging material.
Further, aluminum foil or the like can be attached to block moisture and light from the outside almost completely. The stack is
Extrusion lamination method, coextrusion lamination method,
It can be easily carried out by a multi-layer injection molding method, an adhesion method or the like, and the resulting laminate can be easily further processed into a bag shape or a container shape. Thus, as the packaging material, the laminated humidity-conditioning molded article of the present invention in which a waterproof material is laminated on the outer layer and a moisture-permeable protective material is laminated on the inner layer, if necessary,
Humidity control and moisture absorption effect, its life, durability, light shielding property, antistatic property, safety and stability are improved, and it is more excellent in quality deterioration prevention effect, and more functional that can be used in all usage environments. It is a thing.

【0019】本発明の調湿性組成物は、押出成形、共押
出成形、射出成形、中空成形、押出コ−ティング成形、
架橋発泡成形等の方法により、フィルム状、シ−ト状、
プレ−ト状、袋状、ペレット状、容器状、積層体状等の
形状に加工成形されて調湿性成形品となる。なお、ここ
に容器状とは、容器そのもののみならず、容器の蓋及び
容器とその蓋との組合せをも意味する。
The humidity control composition of the present invention comprises extrusion molding, coextrusion molding, injection molding, blow molding, extrusion coating molding,
By a method such as cross-linking foam molding, a film shape, a sheet shape,
A humidity control molded product is obtained by processing and molding into a plate shape, a bag shape, a pellet shape, a container shape, a laminated body shape or the like. It should be noted that the term "container shape" here means not only the container itself, but also a container lid and a combination of the container and the lid.

【0020】[0020]

【作用】本発明で用いる硫酸マグネシウムは、恒温条件
で吸湿を出発していくと、水和段階が進むにつれて蒸気
圧が上昇し、これに伴い環境の水蒸気の分圧との差が小
さくなり、したがつて吸湿速度は低下していき、その結
果一定の湿度を保ち調湿機能を有する組成物とすること
ができる。
In the magnesium sulfate used in the present invention, when moisture absorption starts under constant temperature conditions, the vapor pressure increases as the hydration stage progresses, and the difference with the partial pressure of environmental water vapor decreases accordingly. Therefore, the rate of moisture absorption decreases, and as a result, a composition having a humidity control function while maintaining a constant humidity can be obtained.

【0021】また、本発明で用いる硫酸マグネシウム
は、湿気を吸収すると、最初に6水塩が生成し、吸湿量
の増加に従い6水塩のみが増え、その間に1〜5水塩の
生成はなく、無水の硫酸マグネシウムが僅かになつた時
点、すなわち吸水率が43〜48%の時に7水塩に変化
する。この事実により、他の水和物形成性の塩を利用し
た乾燥剤と異なり、高吸湿時においても無水物が存在
し、吸湿力を一定に保持し調湿機能のある組成物とな
る。
Further, when magnesium sulfate used in the present invention absorbs moisture, hexahydrate is first produced, and only hexahydrate increases as the amount of moisture absorption increases, and 1-5 pentahydrate is not formed in the meantime. , When the amount of anhydrous magnesium sulfate becomes very small, that is, when the water absorption rate is 43 to 48%, it changes into a heptahydrate. Due to this fact, unlike other desiccants using salts capable of forming hydrates, an anhydride is present even at the time of high moisture absorption, and the composition has a humidity control function by keeping the moisture absorption power constant.

【0022】さらに、本発明で用いる硫酸マグネシウム
は、それ自体がある一定の蒸気圧を示し、外界の水蒸気
の分圧と、自己の蒸気圧とが平衡となるところまで吸湿
を行うことができる。上記の硫酸マグネシウムを樹脂に
練り込んだ場合、樹脂と硫酸マグネシウムの複合体が一
定の蒸気圧を示すようになる。この時の蒸気圧は、硫酸
マグネシウム単体のものと異なり、練り込まれた樹脂の
透湿度によつて影響を受け、樹脂によつて異なつた値と
なる。そうなると当然、平衡に至る点も異なつたものと
なり、吸湿できなくなる平衡湿度も異なつたものとな
り、したがつて、保持すべき一定湿度を樹脂によつて適
宜調整することができる。
Furthermore, the magnesium sulfate used in the present invention itself exhibits a certain constant vapor pressure, and can absorb moisture up to the point where the partial pressure of water vapor in the external environment and its own vapor pressure are in equilibrium. When the above magnesium sulfate is kneaded into the resin, the composite of the resin and magnesium sulfate exhibits a constant vapor pressure. The vapor pressure at this time is different from that of magnesium sulfate alone, and is affected by the moisture permeability of the kneaded resin, and has a different value depending on the resin. In that case, naturally, the point at which equilibrium is reached is different, and the equilibrium humidity at which moisture cannot be absorbed is also different. Therefore, the constant humidity to be held can be adjusted appropriately by the resin.

【0023】[0023]

【実施例】【Example】

実施例1 エチレン−メチルアクリレ−ト共重合体(EMA、密度
0.942g/cm3 )100重量部、無水硫酸マグネ
シウム(平均粒子径4.59μm、比表面積4.0〜
1.5m2 /g)100重量部を混練押出成形機(池貝
鉄工株式会社製PCM45二軸押出機)で混練した後、
ホットカットをしてペレットを作製し、さらにTダイ法
により厚さ0.5mmのシ−トを作製した。比較のため
に、低密度ポリエチレン(密度0.921g/cm3
100重量部とゼオライト(平均粒子径8μm)50重
量部とを同様にして混練し、射出成形機により厚さ2m
mのプレ−トを作製した。同様に比較のために、低密度
ポリエチレンとシリカゲル(粒度200〜300メッシ
ュ)とをゼオライトの場合と同様に混練し、射出成形機
により厚さ2mmのプレ−トを作製した。
Example 1 100 parts by weight of ethylene-methyl acrylate copolymer (EMA, density 0.942 g / cm 3 ), anhydrous magnesium sulfate (average particle diameter 4.59 μm, specific surface area 4.0 to 4.0)
After kneading 100 parts by weight of 1.5 m 2 / g) with a kneading extruder (PCM45 twin screw extruder manufactured by Ikegai Tekko KK),
Hot cutting was performed to produce pellets, and a sheet having a thickness of 0.5 mm was produced by the T-die method. Low density polyethylene (density 0.921 g / cm 3 ) for comparison
100 parts by weight and 50 parts by weight of zeolite (average particle diameter 8 μm) were kneaded in the same manner, and the thickness was 2 m by an injection molding machine.
m plate was prepared. Similarly, for comparison, low-density polyethylene and silica gel (particle size 200 to 300 mesh) were kneaded in the same manner as in the case of zeolite, and a plate having a thickness of 2 mm was produced by an injection molding machine.

【0024】これらのシ−ト及びプレ−トを試料とし、
別々のガラス容器(容量0.9L)に詰め、室温でガラ
ス容器内における吸湿率と時間との関係を測定し、その
結果を図1に示した。
Using these sheets and plates as samples,
They were packed in separate glass containers (capacity 0.9 L) and the relationship between the moisture absorption rate and time in the glass containers was measured at room temperature, and the results are shown in FIG.

【0025】図1の結果から明らかのように、ゼオライ
ト及びシリカゲルを用いた試料のときは、ガラス容器内
の湿度は0%となってしまい、湿度を一定に保つことが
できず、調湿機能がないことがわかる。これに対して無
水硫酸マグネシウムを用いた本発明の試料の場合には、
湿度を19%に保つことができて、調湿機能を有するこ
とがわかる。 実施例2 ポリアミド100重量部と無水硫酸マグネシウム(平均
粒子径4.59μm、比表面積4.0〜1.5m2
g)50重量部とを実施例1において使用した混練押出
成形機で混練した後、ホットカットをしてペレットを作
製し、さらに、Tダイ法により厚さ0.5mmのシ−ト
を作製した。同様の方法によりポリプロピレンと無水硫
酸マグネシウムとから厚さ0.5mmのシ−トを作製し
た。前者及び後者のシ−ト試料を別々のガラス容器(容
量0.9L)に詰め、ガラス容器内の前者及び後者の試
料の調湿力と回復力及び持続力を調べるために、25℃
において一定時間(48時間)内のガラス容器内の密閉
空間における吸湿の回復限度を連続して測定し、前者及
び後者の試料についての結果をそれぞれ図2及び図3に
示した。
As is clear from the results of FIG. 1, in the case of the sample using zeolite and silica gel, the humidity in the glass container was 0%, and the humidity could not be kept constant, and the humidity control function was not achieved. You can see that there is no. On the other hand, in the case of the sample of the present invention using anhydrous magnesium sulfate,
It can be seen that the humidity can be kept at 19% and the humidity control function is provided. Example 2 100 parts by weight of polyamide and anhydrous magnesium sulfate (average particle size 4.59 μm, specific surface area 4.0 to 1.5 m 2 /
g) 50 parts by weight was kneaded with the kneading extruder used in Example 1, hot cut to prepare pellets, and a sheet having a thickness of 0.5 mm was prepared by the T-die method. .. A sheet having a thickness of 0.5 mm was prepared from polypropylene and anhydrous magnesium sulfate by the same method. The former and latter sheet samples were packed in separate glass containers (capacity 0.9 L), and the temperature was adjusted to 25 ° C. in order to examine the humidity control, recovery and sustainability of the former and latter samples in the glass containers.
The recovery limit of moisture absorption in the closed space in the glass container within a fixed time (48 hours) was continuously measured in the above, and the results for the former and latter samples are shown in FIGS. 2 and 3, respectively.

【0026】図2及び図3から明らかのように、本発明
の試料は何れも調湿力があり、回復力もあり、持続力を
有することがわかる。また、熱可塑性樹脂の種類を変え
ることにより本発明においては任意の湿度に調湿し得る
ことが明らかである。 実施例3 (A)低密度ポリエチレン(密度0.921g/c
3 )100重量部と実施例1において使用した無水硫
酸マグネシウム50重量部とを実施例1において使用し
た混練押出成形機で混練した後、ホットカットをしてペ
レットを作製し、さらにインフレ−ション法により、無
水硫酸マグネシウム33%を含有する低密度ポリエチレ
ンフィルムを含む三層フィルムを作製した。この三層の
内容は図4に示すように、外層の50μm厚さの高密度
ポリエチレン層1と、中間層の硫酸マグネシウム33%
含有、50μm厚さの低密度ポリエチレン層2と、内層
の10μm厚さの低密度ポリエチレン層3とからなる、
厚さ110μmの三層インフレ−ションフィルム4であ
つて、さらにこのフィルム4から袋(300×200×
0.11mm)を作製した。 (B)上記の無水硫酸マグネシウムを実施例1で使用し
たエチレン−メチルアクリレ−ト共重合体に33%含有
させて得られた、50μm厚さの、硫酸マグネシウム含
有エチレン−メチルアクリレ−ト共重合体層5を、中間
層として用いた以外は、上記の(A)の場合と同様にし
て三層インフレ−ションフィルムを作製し、その外層に
ポリエチレンテレフタレ−ト(PET)層(厚さ12μ
m)6/Al層(厚さ9μm)7/LDPE層(厚さ1
5μm)8からなるAlコ−トフィルム層をラミネ−ト
して、厚さ146μmのAlコ−トラミネ−トフィルム
9(図5)を作製し、さらにこのフィルム9から袋(3
00×200×0.146mm)を作製した。 (C)外層のHDPE層1及び中間層の硫酸マグネシウ
ム含有LDPE層2の厚さをそれぞれ20μm及び30
μmとした以外は、(A)と同様にして三層インフレ−
ションフィルムを作製し、その外層に、二軸延伸ポリプ
ロピレンフィルムにポリ塩化ビニリデンをコ−ティング
したタイセル化学工業株式会社製のセネンKOP#20
フィルム層(厚さ20μm)10をラミネ−トして、厚
さ80μmのKOPコ−トラミネ−トフィルム11(図
6)を作製し、さらに、このフィルム11から袋(30
0×200×0.08mm)を作製した。
As is clear from FIGS. 2 and 3, it can be seen that the samples of the present invention have a humidity control power, a recovery power, and a sustaining power. Further, it is apparent that the humidity can be adjusted to an arbitrary humidity in the present invention by changing the type of the thermoplastic resin. Example 3 (A) Low-density polyethylene (density 0.921 g / c
m 3 ) 100 parts by weight and 50 parts by weight of anhydrous magnesium sulfate used in Example 1 were kneaded by the kneading extruder used in Example 1, hot cut to prepare pellets, and then inflation. By the method, a three-layer film including a low density polyethylene film containing 33% anhydrous magnesium sulfate was prepared. As shown in FIG. 4, the contents of the three layers are, as shown in FIG. 4, an outer layer of a high-density polyethylene layer 1 having a thickness of 50 μm and an intermediate layer of 33% magnesium sulfate.
Containing a low-density polyethylene layer 2 having a thickness of 50 μm and an inner low-density polyethylene layer 3 having a thickness of 10 μm,
A three-layer inflation film 4 having a thickness of 110 μm, which is further formed from this film 4 into a bag (300 × 200 ×).
0.11 mm) was produced. (B) Magnesium sulfate-containing ethylene-methyl acrylate copolymer layer having a thickness of 50 μm, obtained by containing 33% of the above anhydrous magnesium sulfate in the ethylene-methyl acrylate copolymer used in Example 1. A three-layer inflation film was prepared in the same manner as in the above (A) except that 5 was used as the intermediate layer, and a polyethylene terephthalate (PET) layer (thickness: 12 μm) was formed on the outer layer thereof.
m) 6 / Al layer (thickness 9 μm) 7 / LDPE layer (thickness 1
5 μm) 8 and an Al coat film layer composed of 8 are laminated to form an Al coat laminating film 9 (FIG. 5) having a thickness of 146 μm.
00 × 200 × 0.146 mm) was produced. (C) The thickness of the outer HDPE layer 1 and the thickness of the intermediate magnesium sulfate-containing LDPE layer 2 are 20 μm and 30 respectively.
Three-layer inflation in the same manner as in (A), except for μm
Film produced and coated with polyvinylidene chloride on a biaxially stretched polypropylene film, Senen KOP # 20 manufactured by Taisel Chemical Co., Ltd.
The film layer (thickness 20 μm) 10 is laminated to prepare a KOP coat laminating film 11 (FIG. 6) having a thickness of 80 μm.
0 × 200 × 0.08 mm) was produced.

【0027】上記の(A)、(B)及び(C)に示す袋
内での吸湿繰り返しテストを25℃で行い、それぞれの
調湿機能についての結果を図7、図8及び図9にそれぞ
れ示した。なお比較のために、比較用市販品、すなわ
ち、(A)の袋に対しては市販の0.06mm厚さのポ
リ袋、(B)の袋に対しては市販のアルミコ−ト袋及び
(C)の袋に対しては市販の0.06mm厚さのポリ袋
についても同様のテストを行い、その結果をもそれぞれ
図7、図8及び図9に示した。
The moisture absorption repeating test in the bag shown in (A), (B) and (C) above was conducted at 25 ° C., and the results of the respective humidity control functions are shown in FIGS. 7, 8 and 9, respectively. Indicated. For comparison, a commercially available product for comparison, that is, a commercially available 0.06 mm-thick plastic bag for the bag (A), and a commercially available aluminum coat bag (( The same test was performed on the commercially available 0.06 mm thick polybag for the bag of C), and the results are also shown in FIGS. 7, 8 and 9, respectively.

【0028】図7、図8及び図9に示す結果から明らか
のように、吸湿繰り返しテストにおいて、上記の
(A)、(B)及び(C)の何れの場合も、本発明品は
一定の湿度を保持し調湿機能を示したが、比較用市販品
は調湿機能を示さなかつた。
As is clear from the results shown in FIGS. 7, 8 and 9, in the repeated moisture absorption test, the product of the present invention was not tested in any of the above cases (A), (B) and (C). It showed humidity control function while retaining humidity, but the commercial product for comparison did not show humidity control function.

【0029】さらに、前記したように、練り込まれる樹
脂を変化させることによつて平衡湿度を変え調湿機能を
制御し得ることがわかる。また、上記の(A)、
(B)、(C)の場合のように、硫酸マグネシウムの練
り込まれた層の量や外層を変化させることによつても、
調湿機能の多少の制御が可能である。
Further, as described above, it is understood that the equilibrium humidity can be changed and the humidity control function can be controlled by changing the resin to be kneaded. In addition, the above (A),
As in the case of (B) and (C), by changing the amount of the layer in which magnesium sulfate is kneaded and the outer layer,
Some control of the humidity control function is possible.

【0030】さらに、硫酸マグネシウムを、上記の
(A)のように、低密度ポリエチレンに練り込んだもの
は、上記の(B)のように、エチレン−メチルアクリレ
−ト共重合体に練り込んだものに比べて、樹脂の透湿度
が低いので、(A)のものは、(B)のものより平衡湿
度が高くなっている。(B)のものは、練り込んだ樹脂
がエチレン−メチルアクリレ−ト共重合体という透湿度
の高いものであるので、上記のように、(A)のものに
比べ平衡湿度は低くなるが、(C)のもののように、
(A)と同じ樹脂に練り込んだものであつても、層構成
の変化によって多少異なった平衡湿度となる。
Further, magnesium sulfate is kneaded into low-density polyethylene as in (A) above, and is kneaded into ethylene-methyl acrylate copolymer as in (B) above. Since the resin has a lower water vapor transmission rate than that of (A), the equilibrium humidity of (A) is higher than that of (B). In the case of (B), since the kneaded resin is an ethylene-methyl acrylate copolymer, which has a high moisture permeability, the equilibrium humidity is lower than that of (A) as described above. Like the one in C),
Even if the same resin as (A) is kneaded, the equilibrium humidity will be slightly different depending on the change in the layer structure.

【0031】このように、硫酸マグネシウムと樹脂の組
合せを変えることによって、平衡湿度の異なる種々の調
湿機能を持った調湿性フィルムを得ることができる。
As described above, by changing the combination of magnesium sulfate and the resin, it is possible to obtain a humidity control film having various humidity control functions with different equilibrium humidity.

【0032】実施例4 実施例3において使用した低密度ポリエチレン100重
量部と実施例1において使用した無水硫酸マグネシウム
50重量部とを、実施例1において使用した混練押出成
形機で混練したのち、ホットカットをしてペレットを作
製し、また、実施例1において使用したエチレン−メチ
ルアクリレ−ト共重合体100重量部と実施例1におい
て使用した無水硫酸マグネシウム100重量とから同様
にペレットを作製した。この二種類のペレットから射出
成形機(日精樹脂工業株式会社製PS−20E2VS
E)を用いて500ml容量の広口容器の中蓋(直径
9.2mm、厚さ1mm)の試料二種類を作製し、この
両者の試料につきそれぞれの調湿機能を調べるために、
25℃において広口容器内の密閉空間における吸湿の繰
り返しテストをおこない、その結果を図10にそれぞれ
示した。なお比較のために、比較用一般品についても同
様にテストをおこない、その結果をも図10に示した。
Example 4 100 parts by weight of the low-density polyethylene used in Example 3 and 50 parts by weight of anhydrous magnesium sulfate used in Example 1 were kneaded by the kneading extruder used in Example 1, and then hot. Pellets were prepared by cutting, and pellets were similarly prepared from 100 parts by weight of the ethylene-methyl acrylate copolymer used in Example 1 and 100 parts by weight of anhydrous magnesium sulfate used in Example 1. An injection molding machine (PS-20E2VS manufactured by Nissei Plastic Industry Co., Ltd.)
E) was used to prepare two kinds of samples of the inner lid (diameter 9.2 mm, thickness 1 mm) of a 500 ml capacity wide-mouth container, and in order to investigate the humidity control function of each of these two samples,
Repeated tests of moisture absorption in a closed space in a wide-mouthed container were performed at 25 ° C., and the results are shown in FIG. For comparison, a general comparison product was also tested, and the results are also shown in FIG.

【0033】図10から明らかのように、本発明につい
ての試料は調湿力があるが、比較のための一般品試料は
全く調湿力がないことがわかる。 実施例5 住友化学工業株式会社製低密度ポリエチレン(商品名:
スミカセンF411−1、密度0.921g/cm3
100重量部と市販の関東化学株式会社製硫酸マグネシ
ウム(平均粒子径60μm、比表面積0.3〜3.3m
2 /g)50重量部とを実施例1において使用した混練
押出成形機で混練した後、ホットカットをしてペレット
を作製し、さらに、Tダイ法により厚さ0.5mmのシ
−ト(50mm×50mm×0.5mm)を作製した。
別に、本発明で用いる無水硫酸マグネシウム(平均粒子
径4μm、比表面積3.1〜1.6m2 /g)を使用し
た以外は上記と同じようにして、厚さ0.5mmのシ−
トを作り、上記のシ−トとともに温度25℃、相対湿度
75%の雰囲気のもと吸湿試験をおこなつた。その結果
を図11に示した。
As is apparent from FIG. 10, the sample of the present invention has a humidity control power, but the general-purpose sample for comparison has no humidity control power at all. Example 5 Low density polyethylene manufactured by Sumitomo Chemical Co., Ltd. (trade name:
Sumikathene F411-1, Density 0.921 g / cm 3)
100 parts by weight and commercially available magnesium sulfate manufactured by Kanto Chemical Co., Ltd. (average particle size 60 μm, specific surface area 0.3 to 3.3 m)
50 parts by weight of 2 / g) was kneaded by the kneading extruder used in Example 1, hot cut to prepare pellets, and a sheet having a thickness of 0.5 mm was formed by the T-die method. 50 mm × 50 mm × 0.5 mm) was produced.
Separately, the anhydrous magnesium sulfate (average particle diameter 4 μm, specific surface area 3.1 to 1.6 m 2 / g) used in the present invention was used in the same manner as described above, and a sheet having a thickness of 0.5 mm was used.
A moisture absorption test was conducted under the atmosphere of a temperature of 25 ° C. and a relative humidity of 75% together with the above sheet. The results are shown in Fig. 11.

【0034】図11の結果から明らかのように、平均粒
子径が大きく30μmをこえた前者の市販硫酸マグネシ
ウムを用いて作製したシ−トの場合、後者の平均粒子径
が小さく30μm以下の本発明で使用する硫酸マグネシ
ウムを用いて作製したシ−トに比べて吸湿速度が遅い。
さらに、吸湿後、各シ−ト表面について顕微鏡写真(倍
率100倍)を撮影し、後者の本発明品シ−トについて
の写真を図12として、また前者の市販品シ−トについ
ての写真を図13として示した。図12の本発明品シ−
トの場合には吸湿前に比べ表面が変化していない。これ
に対して、粒子径が大きい市販硫酸マグネシウムは比表
面積の変動が大きく、これを用いた図13の比較用シ−
トの場合には吸湿後、硫酸マグネシウムが溶出し結晶化
を起こしており、吸湿に伴い成形品の膨脹、収縮、亀裂
が発生し、寸法安定性は保持できず実用的な成形品とは
ならなかつた。
As is apparent from the results shown in FIG. 11, in the case of the sheet made of the former commercially available magnesium sulfate having a large average particle size of more than 30 μm, the latter of the present invention having a small average particle size of 30 μm or less. The moisture absorption rate is slower than the sheet produced using magnesium sulfate used in.
Further, after absorbing moisture, a microscopic photograph (magnification of 100) was taken on each sheet surface, the latter photograph of the product of the present invention is shown in FIG. 12, and the former photograph of the commercial product is shown. It is shown as FIG. The product sheet of the present invention in FIG.
In the case of G., the surface has not changed compared to before moisture absorption. On the other hand, the commercially available magnesium sulfate having a large particle size has a large variation in specific surface area, and the comparative sheet of FIG.
In this case, magnesium sulfate elutes and crystallizes after moisture absorption, causing expansion, shrinkage, and cracking of the molded product due to moisture absorption, and dimensional stability cannot be maintained, making it a practical molded product. Nakatsuta.

【0035】本発明で使用する無水硫酸マグネシウム
は、平均粒子径が4μmと細かく、また粒子には微細な
ポアが形成され、成形品の安定性、吸湿に伴う膨脹、収
縮、溶出、亀裂等が発生せず、良好な調湿機能を有する
フィルム、シ−ト、成形品を作製することができた。
The anhydrous magnesium sulfate used in the present invention has a fine average particle diameter of 4 μm, and fine pores are formed in the particles, so that the stability of the molded product, the expansion, shrinkage, elution, cracking due to moisture absorption, etc. It was possible to produce a film, a sheet, and a molded product which did not occur and had a good humidity control function.

【0036】実施例6 エチレン−酢酸ビニル共重合体、ポリエチレン及び炭酸
カルシウムのそれぞれ同重量とアゾイソブチロニトリル
(発泡剤)の必要量とを混合した上層用樹脂材料、なら
びにエチレン−酢酸ビニル共重合体、ポリエチレン及び
実施例1で使用した無水硫酸マグネシウムのそれぞれ同
重量と上記の発泡剤の必要量とを混合した下層用樹脂材
料を用いて、混練発泡成形機により、青色(上層)及び
白色(下層)の二層(両層の厚さは等しい)よりなる、
独立気泡構造の発泡二層品[50mm×50mm×20
mm(厚さ)]の試料を得た。この試料につき、温度2
5℃、相対湿度75%及び温度25℃、相対湿度50%
の両条件下、吸湿率をそれぞれ測定し、その結果を図1
4に示した。
Example 6 A resin material for an upper layer in which the same weight of each of ethylene-vinyl acetate copolymer, polyethylene and calcium carbonate and the required amount of azoisobutyronitrile (foaming agent) were mixed, and ethylene-vinyl acetate copolymer Using a resin material for the lower layer in which the same weight of each of the polymer, polyethylene and anhydrous magnesium sulfate used in Example 1 and the required amount of the above-mentioned foaming agent are mixed, a blue (upper layer) and a white color are obtained by a kneading foam molding machine. It consists of two layers (lower layer) (both layers have the same thickness),
Two-layer foam product with closed cell structure [50 mm x 50 mm x 20
mm (thickness)] was obtained. Temperature 2 for this sample
5 ° C, relative humidity 75% and temperature 25 ° C, relative humidity 50%
The moisture absorption rate was measured under both conditions and the results are shown in Fig. 1.
Shown in FIG.

【0037】図14から明らかのように、上記の発泡二
層品は高い吸湿力を有していた。また、この発泡二層品
は、低湿度の時には吸湿に長時間を要し、また高湿度の
時には吸湿に短時間を要し、調湿機能を有していた。
As is apparent from FIG. 14, the above foamed two-layer article had a high hygroscopic force. Further, this foamed two-layer product had a humidity control function because it required a long time to absorb moisture when the humidity was low and a short time to absorb moisture when the humidity was high.

【0038】実施例7 実施例5で用いた低密度ポリエチレン100重量部、実
施例1で用いた無水硫酸マグネシウム50重量部を、実
施例1で用いた混練押出成形機で混練した後、ホットカ
ットをしてペレットを作製し、さらにTダイ法により厚
さ0.5mm(50mm×50mm×0.5mm)のシ
−トを作製した。比較のために、上記の低密度ポリエチ
レン100重量部と硫酸マグネシウム5水和物(MgS
4 ・5H2 O)50重量部とから上記と同様にしてペ
レットを作製し、さらにTダイ法により上記と同様の厚
さ0.5mmのシ−トを作製した。これらのシ−トを試
料とし、温度25℃、相対湿度75%の条件下で吸湿試
験をおこない、それぞれの吸湿率を測定し比較した結果
を図15に示した。
Example 7 100 parts by weight of the low-density polyethylene used in Example 5 and 50 parts by weight of anhydrous magnesium sulfate used in Example 1 were kneaded by the kneading extruder used in Example 1, and then hot cut. A pellet having a thickness of 0.5 mm (50 mm × 50 mm × 0.5 mm) was produced by the T-die method. For comparison, 100 parts by weight of the above low-density polyethylene and magnesium sulfate pentahydrate (MgS
Pellets were prepared in the same manner as above from 50 parts by weight of O 4 .5H 2 O), and a sheet having a thickness of 0.5 mm similar to the above was prepared by the T-die method. Using these sheets as samples, a moisture absorption test was conducted under the conditions of a temperature of 25 ° C. and a relative humidity of 75%, and the moisture absorption rates were measured and compared. The results are shown in FIG.

【0039】図15の結果から、比較用の硫酸マグネシ
ウム5水和物を含有したシ−ト試料の場合には、本発明
で用いる無水硫酸マグネシウムを含有したシ−ト試料の
場合にくらべて、吸湿速度が遅いことが明らかである。
From the results of FIG. 15, in the case of the sheet sample containing magnesium sulfate pentahydrate for comparison, as compared with the sheet sample containing anhydrous magnesium sulfate used in the present invention, It is clear that the rate of moisture absorption is slow.

【0040】硫酸マグネシウムのように、塩の無水物が
水和物となることによつて吸湿していくものは、塩の水
和状態に応じて一定の蒸気圧を有する。この蒸気圧は、
水和段階が進むにつれて上昇する傾向にある。当然、無
水硫酸マグネシウムの蒸気圧は、5水和物の蒸気圧より
低い値となる。この両者を相対湿度75%、25℃の環
境下に置いたとき両者は速やかに吸湿を開始するが、両
者の吸湿速度は、この環境の水蒸気の分圧と各々自己の
持つ蒸気圧との差によつて決定される。この差が大きけ
れば吸湿速度は速くなり、小さければ遅くなる。よつ
て、吸湿状況は図15に示すようになり、前記したよう
に、硫酸マグネシウム5水和物を含有したシ−ト試料の
場合には、無水硫酸マグネシウムを含有したシ−ト試料
の場合にくらべて、吸湿速度がおそくなる。
A substance such as magnesium sulfate, which absorbs moisture as an anhydride of a salt becomes a hydrate, has a constant vapor pressure depending on the hydration state of the salt. This vapor pressure is
It tends to increase as the hydration stage progresses. Naturally, the vapor pressure of anhydrous magnesium sulfate is lower than the vapor pressure of pentahydrate. When both are placed in an environment of relative humidity of 75% and 25 ° C, they both start to absorb moisture quickly. However, the rate of moisture absorption of both is the difference between the partial pressure of water vapor in this environment and the vapor pressure of its own. It is decided by. If this difference is large, the moisture absorption rate will be fast, and if it is small, it will be slow. Therefore, the hygroscopic state is as shown in FIG. 15, and as described above, in the case of the sheet sample containing magnesium sulfate pentahydrate, in the case of the sheet sample containing anhydrous magnesium sulfate, Compared with this, the moisture absorption rate becomes slower.

【0041】本発明で用いる無水硫酸マグネシウムの場
合には、恒温条件で吸湿を出発していくと、水和段階が
進むにつれて吸湿速度は蒸気圧の上昇に伴い低下してい
き、図15に示すような吸湿曲線を描き、一定の湿度を
保ち調湿機能を有していることがわかる。
In the case of anhydrous magnesium sulfate used in the present invention, when moisture absorption is started under constant temperature conditions, the moisture absorption rate decreases as the vapor pressure increases as the hydration stage progresses, as shown in FIG. It can be seen that such a moisture absorption curve is drawn and that it has a humidity control function while maintaining a constant humidity.

【0042】比較用の硫酸マグネシウム5水和物は樹脂
とともに混練押出成形機で混練を行う時に、混練押出成
形機内にて加温されると自己の持つ水和水を放出し、製
造中の障害が生じ、有効な機能を発揮し得る調湿性組成
物を得ることができず、また、この組成物からフィル
ム、シ−ト、容器等の成形品を作製しようとしても、商
品価値のある調湿性成形品を得ることができなかつた。
The magnesium sulfate pentahydrate for comparison, when it is kneaded with a resin in a kneading extruder, releases its own water of hydration when heated in the kneading extruder, which causes obstacles during production. Occurs, and it is not possible to obtain a humidity control composition capable of exerting an effective function, and even if an attempt is made to form a molded article such as a film, a sheet or a container from this composition, the humidity control with commercial value is obtained. A molded product could not be obtained.

【0043】[0043]

【発明の効果】本発明の調湿性組成物及び調湿性成形品
は以下のような効果を奏する。
The humidity-controlling composition and the humidity-controlling molded article of the present invention have the following effects.

【0044】1)密封した容器、袋等の内部の湿度を一
定に保ち内容物を適度な湿度に保持する機能、すなわち
調湿機能を有し、湿度60%〜10%の範囲で任意の一
定湿度に保持する。
1) It has a function of keeping the internal humidity of a sealed container, bag or the like constant and keeping the contents at an appropriate humidity, that is, a humidity control function, and has an arbitrary constant within a range of humidity 60% to 10%. Keep in humidity.

【0045】2)安定した調湿力、保水力を有し、しか
も腐食性、飛散性、吸湿液化現象による液化漏洩もしく
は水滴の発生などを生じないために調湿剤として優れた
安定性及び使用上の安全性を有している。よって、商品
の酸化等による品質劣化を効果的に防止する。
2) Excellent stability and use as a humidity control agent because it has stable humidity control and water retention and does not cause liquefaction leakage or generation of water droplets due to corrosiveness, scattering, and moisture absorption and liquefaction phenomenon. Has the above safety. Therefore, it is possible to effectively prevent quality deterioration due to oxidation of the product.

【0046】3)使用時に、従来の乾燥剤のように包装
する必要がなく、また袋状、容器状などの形状の包材と
して成形されたものは、包材自体が調湿剤として働き、
上記と同様の調湿効果を発揮するので極めて合理的に働
く。
3) At the time of use, it is not necessary to wrap it like a conventional desiccant, and when it is formed as a bag-shaped or container-shaped packaging material, the packaging material itself functions as a humidity control agent,
Since it exerts the same humidity control effect as above, it works extremely rationally.

【0047】4)吸湿効果が長時間持続する。4) The moisture absorption effect lasts for a long time.

【0048】5)製造及び加工が容易で、優れた工業生
産性を有する。
5) It is easy to manufacture and process and has excellent industrial productivity.

【0049】6)遮光性、帯電防止性を具備する。6) It has a light-shielding property and an antistatic property.

【0050】7)発泡体として得られる発泡調湿性成形
品は、軽量で発泡体内部にまで吸湿効果が及ぶためにさ
らに高い吸湿力をもたらす。
7) The foamed moisture-conditioning molded article obtained as a foam is lightweight and has a higher hygroscopic effect because it has a moisture absorbing effect even inside the foam.

【0051】以上のような効果を奏する本発明の調湿性
組成物及び成形品は、食品、医薬品、化粧品、嗜好品、
精密機械、機械部品等幅広い分野での品質保護のための
優れた調湿剤として使用できるものであつて、画期的な
ものである。
The humidity-controlling composition and molded article of the present invention having the above-mentioned effects are foods, pharmaceuticals, cosmetics, favorite products,
It is an epoch-making product that can be used as an excellent humidity control agent for quality protection in a wide range of fields such as precision machinery and machine parts.

【図面の簡単な説明】[Brief description of drawings]

【図1】本発明の実施例1で得られたシ−ト試料と比較
用プレ−ト試料との調湿機能を比較して示す曲線図。
FIG. 1 is a curve diagram showing the humidity control functions of a sheet sample obtained in Example 1 of the present invention and a comparative plate sample for comparison.

【図2】本発明の実施例2で得られたシ−ト試料の調湿
機能を示す曲線図。
FIG. 2 is a curve diagram showing the humidity control function of the sheet sample obtained in Example 2 of the present invention.

【図3】本発明の実施例2で得られた他のシ−ト試料の
調湿機能を示す曲線図。
FIG. 3 is a curve diagram showing the humidity control function of another sheet sample obtained in Example 2 of the present invention.

【図4】本発明の実施例3で得られた三層インフレ−シ
ョンフィルムの層構成を示す説明図。
FIG. 4 is an explanatory view showing the layer structure of a three-layer inflation film obtained in Example 3 of the present invention.

【図5】本発明の実施例3で得られたAlコ−トラミネ
−トフィルムの層構成を示す説明図。
FIG. 5 is an explanatory view showing the layer structure of the Al co-traminate film obtained in Example 3 of the present invention.

【図6】本発明の実施例3で得られたKOPコ−トラミ
ネ−トフィルムの層構成を示す説明図。
FIG. 6 is an explanatory view showing the layer structure of the KOP co-traminate film obtained in Example 3 of the present invention.

【図7】図4に示すフィルムより作製した本発明品の袋
と比較用市販品の袋との調湿機能を比較して示す曲線
図。
FIG. 7 is a curve diagram showing the humidity control function of the bag of the present invention manufactured from the film shown in FIG. 4 and the bag of the commercial product for comparison in comparison.

【図8】図5に示すフィルムより作製した本発明品の袋
と比較用市販品の袋との調湿機能を比較して示す曲線
図。
FIG. 8 is a curve diagram showing the humidity control function of the bag of the present invention made from the film shown in FIG. 5 and the bag of the commercially available product for comparison in comparison.

【図9】図6に示すフィルムより作製した本発明品の袋
と比較用市販品の袋との調湿機能を比較して示す曲線
図。
9 is a curve diagram showing the humidity control function of the bag of the present invention made from the film shown in FIG. 6 and the bag of the comparative commercial product for comparison.

【図10】本発明の実施例4で得られた広口容器の中蓋
二試料と比較用一般品との調湿機能を比較して示す曲線
図。
FIG. 10 is a curve diagram showing the humidity control functions of two samples of the inner lid of the wide-mouthed container obtained in Example 4 of the present invention and a comparative general product in comparison.

【図11】本発明の実施例5で得られたシ−ト試料と市
販の硫酸マグネシウムを用いて作製した比較用シ−ト試
料との調湿機能を比較して示す曲線図。
FIG. 11 is a curve diagram showing the humidity control functions of the sheet sample obtained in Example 5 of the present invention and a comparative sheet sample prepared by using commercially available magnesium sulfate.

【図12】本発明の実施例5で得られたシ−ト試料につ
いて吸湿後の表面の結晶構造を示す顕微鏡写真図。
FIG. 12 is a micrograph showing a crystal structure of a surface of a sheet sample obtained in Example 5 of the present invention after absorbing moisture.

【図13】本発明の実施例5に示される比較用シ−ト試
料について吸湿後の表面の結晶構造を示す顕微鏡写真
図。
FIG. 13 is a photomicrograph showing the crystal structure of the surface of the comparative sheet sample shown in Example 5 of the present invention after moisture absorption.

【図14】本発明の実施例6で得られた発泡二層品試料
についての吸湿試験結果を示す曲線図。
FIG. 14 is a curve diagram showing the results of a moisture absorption test on a foamed double-layered product sample obtained in Example 6 of the present invention.

【図15】本発明の実施例7で得られた無水硫酸マグネ
シウム含有ポリエチレンシ−ト試料と比較用の硫酸マグ
ネシウム5水和物含有ポリエチレンシ−ト試料との吸湿
速度を比較して示す曲線図。
FIG. 15 is a curve diagram showing the moisture absorption rates of the anhydrous magnesium sulfate-containing polyethylene sheet sample obtained in Example 7 of the present invention and the comparative magnesium sulfate pentahydrate-containing polyethylene sheet sample for comparison. ..

【符号の説明】[Explanation of symbols]

1…HDPE層、2…硫酸マグネシウム含有LDPE
層、3,8…LDPE層、4…三層インフレ−ションフ
ィルム、5…硫酸マグネシウム含有EMA層、6…PE
T層、7…Al層、9…Alコ−トラミネ−トフィル
ム、10…KOP層、11…KOPコ−トラミネ−トフ
ィルム。
1 ... HDPE layer, 2 ... Magnesium sulfate-containing LDPE
Layer, 3, 8 ... LDPE layer, 4 ... Three-layer inflation film, 5 ... Magnesium sulfate-containing EMA layer, 6 ... PE
T layer, 7 ... Al layer, 9 ... Al co-laminate film, 10 ... KOP layer, 11 ... KOP co-laminate film.

Claims (6)

【特許請求の範囲】[Claims] 【請求項1】 熱可塑性樹脂100重量部に対し、式M
gSO4 ・nH2 O(但し0≦n≦3)で表され、かつ
平均粒子径が30μ以下である硫酸マグネシウムを5〜
400重量部配合してなる調湿性組成物。
1. The formula M is added to 100 parts by weight of the thermoplastic resin.
gSO 4 · nH 2 O (provided that 0 ≦ n ≦ 3) and an average particle diameter of 30 μm or less of magnesium sulfate 5 to
A humidity control composition containing 400 parts by weight.
【請求項2】 硫酸マグネシウムが、湿気を吸収する
と、最初に6水塩を生成し、吸湿量の増加に従い6水塩
のみが増加し、その間1〜5水塩が生成せず、無水塩が
僅かになって吸水率が43〜48%になった時点で7水
塩に変化するものである請求項1記載の調湿性組成物。
2. When magnesium sulfate absorbs moisture, it first forms hexahydrate, and as the amount of moisture absorption increases, only hexahydrate increases. The humidity control composition according to claim 1, wherein the moisture control composition is changed to a heptahydrate when the water absorption rate becomes 43 to 48% at a low level.
【請求項3】 発泡剤を含有する請求項1又は請求項2
記載の発泡性調湿性組成物。
3. The method according to claim 1, further comprising a foaming agent.
The foamable humidity control composition described.
【請求項4】 請求項3記載の発泡性調湿性組成物から
得られる発泡調湿性成形品。
4. A foaming and humidity-controlling molded article obtained from the foaming and humidity-controlling composition according to claim 3.
【請求項5】 請求項1又は請求項2記載の調湿性組成
物からなるフィルム状、シ−ト状、袋状、ペレット状も
しくは容器状の調湿性成形品。
5. A film-like, sheet-like, bag-like, pellet-like or container-like humidity-conditioning molded article comprising the humidity-controlling composition according to claim 1 or 2.
【請求項6】 請求項1又は請求項2記載の調湿性組成
物からなる調湿性積層材の少なくとも一種を積層した積
層調湿性成形品。
6. A laminated humidity-conditioning molded article obtained by laminating at least one kind of humidity-controlling laminated material comprising the humidity-controlling composition according to claim 1 or 2.
JP3222442A 1991-08-08 1991-08-08 Moisture conditioning composition and moisture conditioning molded article Pending JPH0539379A (en)

Priority Applications (3)

Application Number Priority Date Filing Date Title
JP3222442A JPH0539379A (en) 1991-08-08 1991-08-08 Moisture conditioning composition and moisture conditioning molded article
TW080108489A TW234136B (en) 1991-08-08 1991-10-29
KR1019910019245A KR940006399B1 (en) 1991-08-08 1991-10-31 Desiccant

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP3222442A JPH0539379A (en) 1991-08-08 1991-08-08 Moisture conditioning composition and moisture conditioning molded article

Publications (1)

Publication Number Publication Date
JPH0539379A true JPH0539379A (en) 1993-02-19

Family

ID=16782465

Family Applications (1)

Application Number Title Priority Date Filing Date
JP3222442A Pending JPH0539379A (en) 1991-08-08 1991-08-08 Moisture conditioning composition and moisture conditioning molded article

Country Status (3)

Country Link
JP (1) JPH0539379A (en)
KR (1) KR940006399B1 (en)
TW (1) TW234136B (en)

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JP5858311B1 (en) * 2015-01-23 2016-02-10 富田製薬株式会社 Hygroscopic inorganic filler-containing polyolefin composition and molded body using the same

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JPS61263640A (en) * 1985-05-17 1986-11-21 Mitsui Toatsu Chem Inc Improved steam-absorbing and-desorbing agent

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JPS5811553A (en) * 1981-07-11 1983-01-22 Katayama Chem Works Co Ltd Easily dispersible composition of water-soluble polymer
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Cited By (16)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH08217913A (en) * 1995-02-15 1996-08-27 Fuji Photo Film Co Ltd Moisture-conditioning/gas-absorbing molding
EP1209097A4 (en) * 1999-07-02 2009-11-11 Hisamitsu Pharmaceutical Co Packaging bag for plaster and packaged plaster
US6991095B1 (en) 1999-07-02 2006-01-31 Hisamitsu Pharmaceutical Co., Inc. Packaging bag for plaster and packaged plaster
JP2004018536A (en) * 2002-06-12 2004-01-22 Toppan Printing Co Ltd Resin composition and laminate and package using the same
JP2004143310A (en) * 2002-10-25 2004-05-20 Toppan Printing Co Ltd Resin composition having drying ability, and laminate and packaging form using the same
JP2006272190A (en) * 2005-03-29 2006-10-12 Jsr Corp Transparent hygroscopic composition, molding, film and its production method
JP5030952B2 (en) * 2006-06-16 2012-09-19 東洋アルミニウム株式会社 Drug packaging material and drug packaging bag
WO2007145322A1 (en) * 2006-06-16 2007-12-21 Toyo Aluminium Kabushiki Kaisha Packaging material and bag for packaging of medicinal product
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KR930003954A (en) 1993-03-22
KR940006399B1 (en) 1994-07-20

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