JP3936717B2 - Manufacturing method of solid bath containing tangible material and humidification / cooling device - Google Patents

Manufacturing method of solid bath containing tangible material and humidification / cooling device Download PDF

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JP3936717B2
JP3936717B2 JP2004515439A JP2004515439A JP3936717B2 JP 3936717 B2 JP3936717 B2 JP 3936717B2 JP 2004515439 A JP2004515439 A JP 2004515439A JP 2004515439 A JP2004515439 A JP 2004515439A JP 3936717 B2 JP3936717 B2 JP 3936717B2
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英利 藤井
悟 長瀬
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関西酵素株式会社
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    • AHUMAN NECESSITIES
    • A61MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61QSPECIFIC USE OF COSMETICS OR SIMILAR TOILETRY PREPARATIONS
    • A61Q19/00Preparations for care of the skin
    • A61Q19/10Washing or bathing preparations
    • AHUMAN NECESSITIES
    • A61MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61KPREPARATIONS FOR MEDICAL, DENTAL OR TOILETRY PURPOSES
    • A61K8/00Cosmetics or similar toiletry preparations
    • A61K8/02Cosmetics or similar toiletry preparations characterised by special physical form
    • AHUMAN NECESSITIES
    • A61MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61KPREPARATIONS FOR MEDICAL, DENTAL OR TOILETRY PURPOSES
    • A61K8/00Cosmetics or similar toiletry preparations
    • A61K8/02Cosmetics or similar toiletry preparations characterised by special physical form
    • A61K8/0216Solid or semisolid forms
    • CCHEMISTRY; METALLURGY
    • C11ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
    • C11DDETERGENT COMPOSITIONS; USE OF SINGLE SUBSTANCES AS DETERGENTS; SOAP OR SOAP-MAKING; RESIN SOAPS; RECOVERY OF GLYCEROL
    • C11D17/00Detergent materials or soaps characterised by their shape or physical properties
    • C11D17/04Detergent materials or soaps characterised by their shape or physical properties combined with or containing other objects
    • C11D17/048Soap or detergent bars or cakes with an inner core consisting of insoluble material
    • CCHEMISTRY; METALLURGY
    • C11ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
    • C11DDETERGENT COMPOSITIONS; USE OF SINGLE SUBSTANCES AS DETERGENTS; SOAP OR SOAP-MAKING; RESIN SOAPS; RECOVERY OF GLYCEROL
    • C11D3/00Other compounding ingredients of detergent compositions covered in group C11D1/00
    • C11D3/0005Other compounding ingredients characterised by their effect
    • C11D3/0052Gas evolving or heat producing compositions
    • AHUMAN NECESSITIES
    • A61MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61KPREPARATIONS FOR MEDICAL, DENTAL OR TOILETRY PURPOSES
    • A61K2800/00Properties of cosmetic compositions or active ingredients thereof or formulation aids used therein and process related aspects
    • A61K2800/20Chemical, physico-chemical or functional or structural properties of the composition as a whole
    • A61K2800/22Gas releasing
    • A61K2800/222Effervescent

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Description

本発明は、玩具等の有形物を包埋した固体入浴剤の製造法及び該製造法に用いる加湿・冷却装置に関し、更に詳細には、有形物の変形を防止して、有形物含有固体入浴剤を加圧成形により、工業的に効率良く生産することが可能な製造法及び該製造法に有効に用いることができる加湿・冷却装置に関する。  The present invention relates to a method for producing a solid bath containing a tangible material such as a toy and a humidifying / cooling device used in the production method, and more particularly, to prevent deformation of the tangible material and to provide a solid bath containing a tangible material. The present invention relates to a production method capable of industrially efficiently producing an agent by pressure molding and a humidification / cooling device that can be effectively used in the production method.

従来から、浴湯に投入した際に酸塩基反応による発泡をともなって溶解する固体入浴剤が広く知られている。該固体入浴剤には、前記酸塩基反応を生じさせるために入浴剤原料として有機酸及び炭酸塩が含まれる。このような有機酸及び炭酸塩を含む固体入浴剤は、通常、空気中の湿気等によっても反応が生じるため、その製造時及び保存時においては湿気を含む水分との接触を充分に防止する必要がある。
前記固体入浴剤は、工業的には通常、打錠成型機を用いて粉末の入浴剤原料を100kgf/cm以上の高圧力で加圧成形する方法により製造されている。このような高圧力で加圧成形された固体入浴剤は、製造直後においてもその表面硬度が高く、取扱い性に優れる。
ところで、近年、入浴剤に娯楽性等を付与することが望まれてきており、種々の娯楽性を有する入浴剤が提案されている。例えば、特開平10−306021号公報、特開昭50−6716号公報、特開昭63−13403号公報又は特開平9−249551号公報において、玩具、植物又は印刷物を内包させた固体入浴剤が提案されている。これらの公報には、入浴剤原料に有形物を混合した後、加圧成形する方法等が提案されている。しかし、上述の従来知られた高圧力による加圧成形法では、玩具等のある程度の大きさを有する有形物を内包させた場合、著しい変形が生じ商品化できず、従って、高圧力成形法により製造される固体入浴剤には、乾燥植物や印刷物等の該高圧力による変形の影響を受け難い有形物でないと内包できないのが実状である。
そこで、変形が生じ易い玩具等を固体入浴剤に内包させる方法として、加圧成形による圧力を低圧にする方法が考えられる。しかし、玩具等が変形しない程度の圧力は、数kgf/cm以下であるため、固体入浴剤自体を所望の形状に成形することが極めて困難であり、また、成形が可能であっても非常に脆いものとなり、工業的にはその管理が煩雑となるため大量生産できず、商品化が極めて困難である。
また、加圧成形機を用いずに手作業により玩具等が内包された固体入浴剤を製造する方法も考えられるが、大量生産できないという問題がある。
2. Description of the Related Art Conventionally, a solid bath agent that dissolves with foaming due to an acid-base reaction when introduced into bath water is widely known. The solid bath agent contains an organic acid and a carbonate as a bath agent raw material in order to cause the acid-base reaction. Since a solid bath containing such an organic acid and carbonate usually reacts due to moisture in the air, it is necessary to sufficiently prevent contact with moisture including moisture during its production and storage. There is.
The solid bath agent is usually produced industrially by a method in which a powder bath raw material is pressure-molded at a high pressure of 100 kgf / cm 2 or more using a tableting molding machine. Such a solid bath agent molded under pressure at a high pressure has a high surface hardness even after production and is excellent in handleability.
By the way, in recent years, it has been desired to impart amusement and the like to bathing agents, and bathing agents having various amusements have been proposed. For example, in Japanese Patent Application Laid-Open No. 10-306021, Japanese Patent Application Laid-Open No. 50-6716, Japanese Patent Application Laid-Open No. 63-13403, or Japanese Patent Application Laid-Open No. 9-249551, a solid bath containing a toy, a plant, or a printed material is provided. Proposed. In these gazettes, a method is proposed in which a tangible material is mixed with a bath salt raw material and then pressure-molded. However, in the above-described conventionally known pressure molding method using high pressure, when a tangible object having a certain size, such as a toy, is included, significant deformation occurs and it cannot be commercialized. In fact, the solid bath preparation to be produced can only be encapsulated if it is a tangible material that is not easily affected by deformation due to the high pressure, such as dried plants and printed matter.
Thus, as a method of enclosing a toy or the like that easily deforms in a solid bath agent, a method of reducing the pressure by pressure molding is conceivable. However, since the pressure at which the toy or the like does not deform is several kgf / cm 2 or less, it is extremely difficult to mold the solid bath agent itself into a desired shape, and even if molding is possible, It is very fragile, and its management is complicated industrially, so it cannot be mass-produced and is extremely difficult to commercialize.
Moreover, although the method of manufacturing the solid bath agent in which the toy etc. were included by manual work without using a press molding machine is also considered, there exists a problem that mass production cannot be performed.

本発明の目的は、玩具等の所定の圧力により変形しうる水不溶性の有形物を内包し、且つ溶解時に酸塩基反応による発泡をともなう固体入浴剤を、該有形物の変形を抑制・防止し、加圧成形法により効率良く、工業的に大量生産しうる有形物含有固体入浴剤の製造法を提供することにある。
本発明の別の目的は、本発明の製造法を実施するにあたり、成形物の表面層を加湿する工程(E)と、成形物を冷却する工程(F)とを、連続的に、且つ効率良く実施しうる加湿・冷却装置を提供することにある。
本発明によれば、発泡性成分としての有機酸及び炭酸塩を含む粉末原料、及び結着性液状物を混合して湿潤粉末原料を準備する工程(A)と、所定圧力により変形しうる水不溶性の有形物、及び工程(A)で準備した湿潤粉末原料を、加圧成形するための容器内に、該有形物が湿潤粉末原料に内包されるように入れる工程(B)と、工程(B)において容器内に収容された有形物及び湿潤粉末原料を、所定形状の型を用いて0.5〜10kgf/cmの圧力により加圧成形する工程(C)と、工程(C)により加圧成形された成形物を前記容器内から取出す工程(D)と、得られた成形物の表面層を加湿する工程(E)と、工程(E)に続いて成形物を5℃以下に冷却する工程(F)とを少なくとも含む有形物含有固体入浴剤の製造法が提供される。
また本発明によれば、前記有形物含有固体入浴剤の製造法に用いる加湿・冷却装置であって、加圧成形された成形物をライン上で搬送する搬送手段と、前記成形物を加湿する加湿手段と、前記成形物を冷却する冷却手段とを備え、
前記加湿手段が、成形物の搬入口及び搬出口を有する加湿トンネル構造体と、該加湿トンネル構造体内の所定空間を加湿しうる加湿器とを備え、
前記冷却手段が、成形物の搬入口及び搬出口を有する冷却トンネル構造体と、該冷却トンネル構造体内の所定空間を冷却しうる冷却器とを備え、前記冷却トンネル構造体が、前記冷却器により冷却する所定空間内の冷気を保持し、且つ成形物の通過を可能にした可撓性の冷気遮蔽手段を、前記搬入口側及び搬出口側に各々少なくとも1つずつ有し、
前記加湿手段と前記冷却手段とを、前記搬送手段のライン上にこの順に配置した加湿・冷却装置が提供される。
An object of the present invention is to suppress or prevent deformation of a tangible object by incorporating a solid bathing agent containing water-insoluble tangible material that can be deformed by a predetermined pressure such as a toy and having foaming due to an acid-base reaction when dissolved. Another object of the present invention is to provide a method for producing a tangible-containing solid bath that can be efficiently mass-produced industrially by a pressure molding method.
Another object of the present invention is to continuously and efficiently perform the step (E) of humidifying the surface layer of the molded product and the step (F) of cooling the molded product in carrying out the production method of the present invention. An object of the present invention is to provide a humidifying / cooling device that can be well implemented.
According to the present invention, the step (A) of preparing a wet powder raw material by mixing a powder raw material containing an organic acid and carbonate as a foaming component, and a binding liquid, and water that can be deformed by a predetermined pressure. The insoluble tangible material and the wet powder raw material prepared in step (A) are placed in a container for pressure molding so that the tangible material is contained in the wet powder raw material (B), In step B), the tangible material and the wet powder raw material housed in the container are pressure-molded with a pressure of 0.5 to 10 kgf / cm 2 using a mold having a predetermined shape, and step (C). The step (D) of taking out the pressure-molded molded product from the container, the step (E) of humidifying the surface layer of the obtained molded product, and the step (E) to 5 ° C. or lower And a method for producing a tangible-containing solid bath containing at least a step (F) of cooling. Provided.
Further, according to the present invention, there is provided a humidifying / cooling device for use in the method for producing the tangible material-containing solid bath agent, the conveying means for conveying the pressure-formed molded product on a line, and the humidifying the molded product. Humidifying means, and cooling means for cooling the molded product,
The humidifying means includes a humidifying tunnel structure having a carry-in port and a carry-out port for a molded product, and a humidifier capable of humidifying a predetermined space in the humidifying tunnel structure,
The cooling means comprises a cooling tunnel structure having a carry-in port and a carry-out port for a molded product, and a cooler capable of cooling a predetermined space in the cooling tunnel structure, and the cooling tunnel structure is formed by the cooler. Having at least one flexible cold air shielding means for holding the cold air in a predetermined space to be cooled and allowing the molded product to pass therethrough on each of the carry-in side and the carry-out side;
There is provided a humidifying / cooling device in which the humidifying means and the cooling means are arranged in this order on the line of the conveying means.

図1は、本発明の加湿・冷却装置の構造を説明するための概略図である。
発明の好ましい実施の態様
以下本発明を更に詳細に説明する。
本発明の有形物含有固体入浴剤の製造法では、まず、発泡性成分としての有機酸及び炭酸塩を含む粉末原料、及び結着性液状物を混合して湿潤粉末原料を準備する工程(A)を行う。
前記粉末原料に含まれる有機酸及び炭酸塩は、固体入浴剤の入浴剤原料を浴湯中で速やかに崩壊、溶解させる作用、更に、溶解により発生する炭酸ガスに基づく温浴効果を期待して配合できる。有機酸としては、例えば、酒石酸、フマル酸、クエン酸、コハク酸、アジピン酸が挙げられる。炭酸塩としては、例えば、炭酸ナトリウム、炭酸水素ナトリウム、セスキ炭酸ナトリウム、これらのカリウム塩が挙げられる。有機酸及び炭酸塩を配合する場合は、入浴剤原料が水分を実質的に含まないように注意する必要がある。有機酸及び炭酸塩の配合割合は、重量比で通常1:1又はこれに近い割合が望ましい。
前記粉末原料は、有機酸及び炭酸塩以外の他の成分を含んでいても良い。例えば、比重調整剤、酵素、界面活性剤、水溶性香料、油溶性香料、色素、各種薬効作用成分、温泉作用成分又はこれらの混合物が挙げられる。各配合割合は所望の目的に応じて適宜決定できる。
前記比重調整剤としては、例えば、無水硫酸ナトリウムが挙げられる。該比重調整剤の含有割合は、得られる有形物含有固体入浴剤を浴湯に投入した直後に浴湯中に沈降する割合、即ち、該固体入浴剤の比重が浴湯の比重より高くなる割合が好ましい。また、酵素、界面活性剤、色素、各種薬効作用成分、温泉作用成分は、所望の目的に応じて公知成分等から適宜選択できる。
前記粉末原料の調製は、各成分を混合撹拌する方法等により行うことができる。この際、例えば、有機酸、香料等の液状成分は、その混合割合及び混合順序等を適宜選択し、最終的に粉末原料となるように他の粉末成分に混合すれば良い。得られる粉末原料は、その粒度を均一に調整することが好ましく、通常、0.5〜5.0mmメッシュの篩を通過させて粒度調整することができる。
前記結着性液状物は、後述する低圧による加圧成形であっても前記粉末原料の成形を可能にし、且つ得られる固体入浴剤の衝撃による割れ等を抑制・防止しうる成分であって、従来の100kgf/cm以上の高圧力で加圧成形するための入浴剤粉末原料においては必ずしも配合されない成分である。結着性液状物は、結着剤及び該結着剤の溶剤を含む。
前記結着剤としては、例えば、ポリエチレングリコール(PEG)、ポリプロピレングリコール、ソルビトール、マンニトール、ブドウ糖、ショ糖又はこれらの混合物が挙げられる。特にPEGの使用が好ましい。PEGの平均分子量は、成形性が良好な点で500〜3700が好ましい。該所望分子量のPEGとしては、例えば、市販品、又は市販品の混合物が挙げられる。
前記結着剤の溶剤としては、例えば、エチレングリコール、プロピレングリコール、1,3−ブチレングリコール、ジエチレングリコール、ジプロピレングリコール、グリセリン、ペンタエリスリトールが挙げられる。特に、PEGの溶剤としては、ジプロピレングリコール及び/又は1,3−ブチレングリコールが好ましい。
前記湿潤粉末原料の調製は、前記粉末原料と前記結着性液状物とを所望の混合割合で混合撹拌することにより得ることができる。この際、本発明の所望の効果を損なわない範囲で粉末原料及び結着性液状物以外の成分を含ませることも可能である。得られる湿潤粉末原料は、その粒度を均一に調整することが好ましく、通常、0.5〜5.0mmメッシュの篩を通過させて粒度調整することができる。ここで、湿潤粉末原料とは、粉末形態が維持され、その表面が結着性液状物により湿っている状態の粉末を意味する。
前記湿潤粉末原料を調製する際の粉末原料及び結着性液状物の混合割合は、各原料の種類に応じて適宜選択できるが、粉末原料:結着性液状物が重量比で1:0.05〜1程度が好ましい。
本発明の製造法では、次に、所定圧力により変形しうる水不溶性の有形物、及び工程(A)で準備した湿潤粉末原料を、加圧成形するための容器内に、該有形物が湿潤粉末原料に内包されるように入れる工程(B)を行う。
前記所定圧力により変形しうる水不溶性の有形物としては、例えば、10kgf/cmを超える圧力により加圧成形した際に変形して完全に復元しない、プラスチック製の玩具等が挙げられる。該有形物の大きさ及び形状は特に限定されない。有形物の大きさは、有形物の外表面と、得られる固体入浴剤の外表面との間の厚さが好ましくは1cm以上の大きさとなるように、得られる固体入浴剤の大きさに応じて決定することが好ましい。有形物の比重は特に限定されないが、固体入浴剤が溶解した際に浴湯面を浮遊するように、浴湯の比重以下が好ましい。
工程(B)において、加圧成形するための容器は、加圧成形可能な容器であれば良く、その形状は特に限定されない。
前記容器内に入れる湿潤粉末原料の量は、工程を煩雑化させないために、得られる固体入浴剤の1個分の湿潤粉末原料全量が好ましい。
工程(B)において、前記容器内に有形物と湿潤粉末原料とを入れるにあたっては、該有形物が湿潤粉末原料に内包されるように入れる方法であれば特に限定されず、原料の入れる順序を適宜選択する方法等により実施できる。
本発明の製造法では、次に、工程(B)において容器内に収容された有形物及び湿潤粉末原料を、所定形状の型を用いて特定の低圧力により加圧成形する工程(C)を行う。
工程(C)の加圧成形は、得られる成形物の形状に応じて、該形状としうる金型等の型を選択し、1方向若しくは2方向から加圧することにより行うことができる。成形物の形状としては、例えば、タマゴ形状、楕円状、キューブ状、三角柱、星型柱、人形等の複雑形状等が挙げられる。
前記加圧は、通常、1段階で行うことができるが、内包される有形物が複雑形状等の場合においては、該有形物と湿潤粉末原料との間に空洞が生じないように1段階目の加圧を2回目移行の加圧よりも低圧により行う2段階以上の加圧によっても行うことができる。
工程(C)における加圧は、通常、0.5〜10kgf/cm、好ましくは1〜5kgf/cmで行うことができる。圧力が10kgf/cmを超える場合には内包される有形物の変形を抑制・防止することができず、0.5kgf/cm未満では成形が困難である。
本発明の製造法では、次に、工程(C)により加圧成形された成形物を前記容器内から取出す工程(D)を行う。取出し方法は特に限定されないが、得られる成形物は非常に脆いので次工程に供するにあたりその取扱いは注意を要する。
本発明の製造法では、次に、得られた成形物の表面層を加湿する工程(E)を行い、続いて成形物を0℃以下に冷却する工程(F)を行う。
工程(D)により容器から取出された成形物は、有機酸及び炭酸塩を含むので工程(E)の加湿により表面層を中性塩にすることができる。このように、表面層を中性塩にすることにより、非常に脆い成形物の表面硬度を速やかに向上させることができ、続いて行う工程(F)による冷却によって、成形物内部における有機酸及び炭酸塩の反応を防止し、更なる表面硬度の向上を促進すると共に、工程(E)における加湿による余分な水分を速やかに除去し、その後の取扱いを容易にできる。また、その後の乾燥や保存における空気との接触による成形物の表面劣化も有効に抑制・防止することができる。
工程(E)において加湿は、例えば、超音波加湿器等により発生させた霧状水を噴霧する方法、成形物をベルトコンベアに載せ、所定速度で霧状水雰囲気の室内を通過させる方法等により行うことができる。該加湿は、成形物の表面層が中性塩となるように通常、10秒間〜2分間行うことが好ましい。
前記工程(F)の冷却は、5℃以下、通常+5〜−10℃、好ましくは+2〜−5℃、特に好ましくは0〜−5℃程度の温度で行うことができる。冷却時間は、長い方が好ましいが、生産効率を考慮した場合、通常1〜30分間、好ましくは2〜20分間程度である。該冷却は、工程(E)に続いて、例えば、成形物をベルトコンベアに載せ、所定速度で冷却室内を通過させる方法等により行うことができる。
前記表面を中性塩とするために加湿を行う工程(E)を行わずに前記冷却のための工程(E)を行っても表面硬度の向上はほとんど見られない。一方、工程(E)と工程(F)との順番を逆にした場合も所望の効果が望めない。
本発明の製造法では、上記工程(A)〜(F)により所望の固体入浴剤を製造できるが、製造直後においては、含有される結着剤等が完全に乾燥されていないので、時間経過と共に硬度が高くなる。従って、前記工程(F)の後に乾燥工程を行うこともできるが、前記工程(E)及び(F)により成形物にある程度の硬度が付与されているので、特に乾燥工程を行わずに工程(F)の後に成形物を包装する工程を行うこともできる。該包装は、例えば、光不透過性であり、且つ密閉可能な袋状又は通気性を有する袋状の包装材により得られた固体入浴剤を包装することにより実施できる。該包装材としては、例えば、アルミ箔等の袋状物、細孔を有する袋状物が挙げられる。また、固体入浴剤を袋状の包装材中に入れ、食品分野で使用される減圧装置により減圧し、密封包装することもできる。
また、前記包装の前に、得られる固体入浴剤の保存時、輸送時、使用時における割れや欠損を有効に防止するために、該固体入浴剤を個別にシュリンク処理することもできる。シュリンク処理は公知の材料を用いて行なうことができる。
本発明の製造法では、本発明の所望の目的が損なわれない範囲で、更に所望の効果や他の効果を向上させるために上記各工程以外の工程又は操作を含んでいても良い。
本発明の製造法により得られる有形物含有固体入浴剤は、浴湯に投入することにより有形物の廻りの入浴剤原料が浴湯に分散・溶解し、所望時間経過後、水不溶性有形物が浴湯中若しくは浴湯面に現れる態様が好ましい。
本発明の加湿・冷却装置は、上記本発明の製造法において、工程(D)で取出した加圧成形された成形物に対して、工程(E)及び工程(F)を実施するための加湿・冷却装置である。本発明の加湿・冷却装置の好ましい態様について、以下に図面を参照して説明するが、本発明の装置はこれに限定されない。
図1は、本発明の加湿・冷却装置10の一実施態様を示す概略図であって、該装置10は、加圧成形された成形物18をライン上で搬送する搬送手段としてのベルトコンベア11と、前記成形物18を加湿する、加湿トンネル構造体12及び加湿器14からなる加湿手段と、前記加湿手段から搬出された成形物18を冷却する、冷却トンネル構造体15及び冷却器17とを備える。
前記加湿トンネル構造体12は、成形物18の搬入口12a及び搬出口12bを有する。ここで、該搬入口12aの内側及び搬出口12bの内側それぞれには、湿気遮蔽手段としての可撓性のプラスチック製シートが加湿トンネル構造体12の天井面から吊るされていてもよい。これらシートには、成形物18の通過を可能にし、且つ通過後においては元の形態に復元し、湿気を所定空間に保持するための下方から上方に複数のスリットが設けられていることが好ましい。このような湿気遮断手段としてのシートは、湿気により水滴が付着し、成形物18に対して好ましくない作用を示す場合があるので、必ずしも設けることが好ましいとは限らない。
加湿器14は、加湿トンネル構造体12内を所望の加湿状態に加湿しうるものであって、通常、加湿率を制御しうる制御部を有する。該加湿器14は、常温以下の霧状水が発生する超音波加湿器であることが好ましい。
前記冷却トンネル構造体15は、成形物18の搬入口15a及び搬出口15bを有し、該搬入口15aの内側及び搬出口15bの内側それぞれには、冷気遮蔽手段としての可撓性のプラスチック製シート16が冷却トンネル構造体15の天井面から吊るされている。これらシート16には、成形物18の通過を可能にし、且つ通過後においては元の形態に復元し、冷気を後述する所定空間に保持するための下方から上方に複数のスリット16aが設けられている。図1の例では、前記各シート16が、搬入口15aの内側及び搬出口15bの内側それぞれに1枚ずつ設けられているが、冷気の遮断をより効率的に行うためには、搬入口15aの内側及び搬出口15bの内側それぞれに、前記シート16を複数、例えば、搬入口15aの内側にシート16を3枚、搬出口15bの内側にシート16を4枚設けた態様等が好ましく挙げられる。
冷却器17は、冷却トンネル構造体15の天井面、側面及び前記シート16で囲まれた所定空間15c内を所望の冷気状態に冷却しうるものであって、通常、冷却温度を制御しうる制御部を有する。該冷却器17は、前記所定空間15c内を+5〜−10℃程度に保持しうる冷却能力を有する装置が好ましい。
図1に示す加湿・冷却装置10においては、加湿トンネル構造体12及び冷却トンネル構造体15を、ベルトコンベア11上に離隔して配置しているが、該離隔の距離は適宜選択でき、また、離隔せずに接触させて配置することも可能である。
次に、図1に示す加湿・冷却装置10の作用を説明する。
本発明の製造法において、上述の工程(A)〜(D)を実施して得られた成形物18は、加湿・冷却装置10のベルトコンベア11上を搬送され、まず、予め加湿器14により所望の湿気状態に保持されている加湿トンネル構造体12の搬入口12aを通過し、該構造体12内を通って、搬出口12bから搬出される。この際、ベルトコンベア11の速度及び加湿トンネル構造体12の長さを調整し、該構造体12内を通過する成形物18の通過時間を調整することにより、成形物18の表面層を所定の中性塩の層とすることができる。
上記加湿された成形物18は、次いで、冷却トンネル構造体15の搬入口15a及びシート16を通過して所定空間15c内に進む。所定空間15c内は、予め冷却器17により5℃以下の所望温度に保持されている。前記成形物18がシート16を通過する際に所定空間15cは一時的に開放系となるが、通過後にシート16が復元し、該空間15cを実質的に閉鎖系に戻すので、所定空間15c内は、効率良く所望の冷却温度状態に保たれる。ベルトコンベア11の速度及び所定空間15cの長さを調整し、所定空間15c内を通過する成形物18の通過時間を調整することにより、成形物18の表面層を所望の冷却及び乾燥状態とし、成形物18の表面硬度を効率良く向上させることができる。
表面硬度が向上された成形物18は、搬出口15b側のシート16及び該搬出口15bを通過して、冷却トンネル構造体15の外に搬出される。
本発明の加湿・冷却装置10においては、所望に応じて冷却トンネル構造体15の後方に、成形物18のシュリンク装置及び/又は包装用装置を設置することも可能である。
FIG. 1 is a schematic view for explaining the structure of the humidifying / cooling device of the present invention.
Preferred Embodiments of the Invention The present invention will be described in more detail below.
In the method for producing a tangible material-containing solid bath agent of the present invention, first, a powder raw material containing an organic acid and carbonate as foaming components and a binding liquid material are mixed to prepare a wet powder raw material (A )I do.
The organic acid and carbonate contained in the powder raw material are formulated with the expectation of the action of rapidly disintegrating and dissolving the bath agent raw material of the solid bath agent in the bath water, and further the warm bath effect based on the carbon dioxide gas generated by the dissolution. it can. Examples of the organic acid include tartaric acid, fumaric acid, citric acid, succinic acid, and adipic acid. Examples of the carbonate include sodium carbonate, sodium hydrogen carbonate, sodium sesquicarbonate, and potassium salts thereof. When blending organic acids and carbonates, care must be taken that the bathing agent ingredients are substantially free of moisture. The mixing ratio of the organic acid and the carbonate is preferably 1: 1 or a ratio close to this by weight ratio.
The powder raw material may contain components other than organic acids and carbonates. For example, specific gravity adjusting agents, enzymes, surfactants, water-soluble fragrances, oil-soluble fragrances, pigments, various medicinal effect ingredients, hot spring action ingredients, or mixtures thereof may be mentioned. Each blending ratio can be appropriately determined according to the desired purpose.
Examples of the specific gravity adjuster include anhydrous sodium sulfate. The content ratio of the specific gravity adjusting agent is the ratio of sedimentation in the bath water immediately after the obtained tangible material-containing solid bath agent is added to the bath water, that is, the ratio in which the specific gravity of the solid bath agent is higher than the specific gravity of the bath water. Is preferred. Moreover, an enzyme, surfactant, a pigment | dye, various medicinal effect components, and a hot spring action component can be suitably selected from well-known components etc. according to the desired objective.
The powder raw material can be prepared by a method of mixing and stirring each component. At this time, for example, liquid components such as organic acids and fragrances may be appropriately selected in terms of the mixing ratio, mixing order, etc., and mixed with other powder components so as to finally become powder raw materials. It is preferable to adjust the particle size of the obtained powder raw material uniformly. Usually, the particle size can be adjusted by passing through a 0.5 to 5.0 mm mesh sieve.
The binding liquid material is a component that enables molding of the powder raw material even under pressure molding at a low pressure, which will be described later, and can suppress and prevent cracking due to impact of the obtained solid bath agent, It is a component that is not necessarily blended in a conventional bath powder powder material for pressure molding at a high pressure of 100 kgf / cm 2 or more. The binding liquid includes a binder and a solvent for the binder.
Examples of the binder include polyethylene glycol (PEG), polypropylene glycol, sorbitol, mannitol, glucose, sucrose, or a mixture thereof. Particularly preferred is the use of PEG. The average molecular weight of PEG is preferably 500 to 3700 in terms of good moldability. Examples of the PEG having the desired molecular weight include a commercially available product or a mixture of commercially available products.
Examples of the solvent for the binder include ethylene glycol, propylene glycol, 1,3-butylene glycol, diethylene glycol, dipropylene glycol, glycerin, and pentaerythritol. In particular, as a solvent for PEG, dipropylene glycol and / or 1,3-butylene glycol are preferable.
The wet powder raw material can be prepared by mixing and stirring the powder raw material and the binding liquid material at a desired mixing ratio. At this time, it is also possible to include components other than the powder raw material and the binding liquid within a range that does not impair the desired effect of the present invention. The obtained wet powder raw material is preferably adjusted to have a uniform particle size, and can usually be adjusted by passing it through a 0.5 to 5.0 mm mesh sieve. Here, the wet powder raw material means a powder in a state where the powder form is maintained and the surface is wetted by the binding liquid material.
The mixing ratio of the powder raw material and the binding liquid material in preparing the wet powder raw material can be appropriately selected according to the type of each raw material, but the powder raw material: binding liquid material is 1: 0. About 05-1 is preferable.
In the production method of the present invention, the water-insoluble tangible material that can be deformed by a predetermined pressure and the wet powder raw material prepared in step (A) are then wetted in a container for pressure molding. A step (B) is performed so as to be included in the powder raw material.
Examples of the water-insoluble tangible material that can be deformed by the predetermined pressure include plastic toys that are not deformed and completely restored when pressure-molded by a pressure exceeding 10 kgf / cm 2 . The size and shape of the tangible object are not particularly limited. The size of the tangible object depends on the size of the obtained solid bath so that the thickness between the outer surface of the tangible object and the outer surface of the obtained solid bath is preferably 1 cm or more. Is preferably determined. The specific gravity of the tangible material is not particularly limited, but is preferably less than the specific gravity of the bath water so that the surface of the bath water floats when the solid bath agent dissolves.
In the step (B), the container for pressure molding may be any container that can be pressure-molded, and the shape thereof is not particularly limited.
The amount of the wet powder raw material to be put in the container is preferably the total amount of the wet powder raw material for one of the obtained solid bath agents so as not to complicate the process.
In the step (B), the tangible material and the wet powder raw material are placed in the container without any particular limitation as long as the tangible material is contained in the wet powder raw material. It can implement by the method etc. which select suitably.
In the production method of the present invention, next, the step (C) of pressure-molding the tangible material and the wet powder raw material contained in the container in the step (B) with a specific low pressure using a mold having a predetermined shape. Do.
The pressure molding in the step (C) can be performed by selecting a mold such as a mold that can be shaped according to the shape of the obtained molded product and pressurizing from one direction or two directions. Examples of the shape of the molded product include an egg shape, an ellipse shape, a cube shape, a triangular prism, a star column, and a complicated shape such as a doll.
The pressurization can usually be performed in one step. However, when the tangible material to be included is a complicated shape, the first step is performed so that no cavity is formed between the tangible material and the wet powder raw material. The pressurization can be performed by two or more stages of pressurization performed at a lower pressure than the pressurization of the second transition.
The pressurization in the step (C) can be usually performed at 0.5 to 10 kgf / cm 2 , preferably 1 to 5 kgf / cm 2 . If the pressure exceeds 10 kgf / cm 2 , deformation of the contained tangible material cannot be suppressed / prevented, and if it is less than 0.5 kgf / cm 2 , molding is difficult.
In the production method of the present invention, next, the step (D) of taking out the molded product pressure-molded in the step (C) from the inside of the container is performed. The take-out method is not particularly limited, but the molded product obtained is very fragile, so that it needs to be handled with care in the next step.
In the production method of the present invention, next, the step (E) of humidifying the surface layer of the obtained molded product is performed, and then the step (F) of cooling the molded product to 0 ° C. or lower is performed.
Since the molded product taken out from the container in the step (D) contains an organic acid and a carbonate, the surface layer can be made a neutral salt by humidification in the step (E). Thus, by making the surface layer into a neutral salt, the surface hardness of the very brittle molding can be quickly improved, and the organic acid and the inside of the molding can be cooled by cooling in the subsequent step (F). While preventing the reaction of carbonate and promoting further improvement of the surface hardness, excess water due to humidification in the step (E) can be quickly removed to facilitate subsequent handling. Further, surface deterioration of the molded product due to contact with air during subsequent drying or storage can be effectively suppressed / prevented.
In step (E), humidification is performed by, for example, a method of spraying mist water generated by an ultrasonic humidifier or the like, a method of placing a molded product on a belt conveyor, and passing the interior of the mist water atmosphere at a predetermined speed. It can be carried out. The humidification is usually preferably performed for 10 seconds to 2 minutes so that the surface layer of the molded product becomes a neutral salt.
The cooling in the step (F) can be performed at a temperature of about 5 ° C. or less, usually +5 to −10 ° C., preferably +2 to −5 ° C., particularly preferably about 0 to −5 ° C. The cooling time is preferably longer, but is usually about 1 to 30 minutes, preferably about 2 to 20 minutes when considering production efficiency. Following the step (E), the cooling can be performed, for example, by a method in which a molded product is placed on a belt conveyor and passed through a cooling chamber at a predetermined speed.
Even if the step (E) for cooling is performed without performing the step (E) of humidifying the surface to make a neutral salt, the surface hardness is hardly improved. On the other hand, when the order of the step (E) and the step (F) is reversed, a desired effect cannot be expected.
In the production method of the present invention, a desired solid bath agent can be produced by the steps (A) to (F). However, immediately after the production, the contained binder and the like are not completely dried, so that time elapses. As the hardness increases. Therefore, although a drying process can also be performed after the said process (F), since a certain amount of hardness is provided to the molding by the said processes (E) and (F), a process (without performing a drying process in particular) A step of packaging the molded product after F) can also be performed. The packaging can be carried out, for example, by packaging a solid bath obtained by a bag-like packaging material that is light-impermeable and sealable or has air permeability. Examples of the packaging material include bag-like materials such as aluminum foil and bag-like materials having pores. Alternatively, the solid bath agent can be put into a bag-shaped packaging material, and the pressure can be reduced by a pressure reducing device used in the food field, and the package can be sealed and packaged.
In addition, before the packaging, in order to effectively prevent cracks and defects during storage, transportation and use of the obtained solid bath agent, the solid bath agent can be individually subjected to a shrink treatment. The shrink process can be performed using a known material.
In the production method of the present invention, steps or operations other than the above steps may be included in order to further improve desired effects and other effects within a range where the desired object of the present invention is not impaired.
The tangible material-containing solid bathing agent obtained by the production method of the present invention disperses and dissolves the bathing agent raw material around the tangible material in the bath water by adding it to the bath water. A mode that appears in the bath or on the bath surface is preferred.
The humidification / cooling device of the present invention is a humidifier for performing the step (E) and the step (F) on the pressure-molded product taken out in the step (D) in the production method of the present invention. -Cooling device. Although the preferable aspect of the humidification / cooling apparatus of this invention is demonstrated with reference to drawings below, the apparatus of this invention is not limited to this.
FIG. 1 is a schematic view showing an embodiment of a humidifying / cooling device 10 according to the present invention. The device 10 is a belt conveyor 11 as a conveying means for conveying a pressure-formed molded product 18 on a line. A humidifying means comprising a humidifying tunnel structure 12 and a humidifier 14 for humidifying the molded product 18; and a cooling tunnel structure 15 and a cooler 17 for cooling the molded product 18 carried out from the humidifying means. Prepare.
The humidifying tunnel structure 12 has a carry-in port 12 a and a carry-out port 12 b for the molded product 18. Here, a flexible plastic sheet as a moisture shielding means may be hung from the ceiling surface of the humidifying tunnel structure 12 inside the carry-in entrance 12a and the inside of the carry-out exit 12b. These sheets are preferably provided with a plurality of slits from the bottom to the top in order to allow the molded product 18 to pass through and to restore the original form after the passage and to keep moisture in a predetermined space. . Such a sheet as a moisture blocking means is not always preferable to be provided because water droplets adhere to the moisture and may exhibit an undesirable effect on the molded product 18.
The humidifier 14 can humidify the inside of the humidifying tunnel structure 12 to a desired humidified state, and usually has a control unit that can control the humidification rate. The humidifier 14 is preferably an ultrasonic humidifier that generates atomized water at room temperature or lower.
The cooling tunnel structure 15 has a carry-in port 15a and a carry-out port 15b for the molded product 18, and each of the inside of the carry-in port 15a and the inside of the carry-out port 15b is made of flexible plastic as a cold air shielding means. The sheet 16 is suspended from the ceiling surface of the cooling tunnel structure 15. These sheets 16 are provided with a plurality of slits 16a from the lower side to the upper side for allowing the molded product 18 to pass therethrough and restoring the original form after the passage and holding the cool air in a predetermined space to be described later. Yes. In the example of FIG. 1, one sheet 16 is provided on each of the inside of the carry-in port 15a and the inside of the carry-out port 15b. However, in order to more efficiently block the cold air, the carry-in port 15a is provided. Preferably, a plurality of sheets 16, for example, three sheets 16 inside the carry-in port 15a and four sheets 16 inside the carry-out port 15b are provided on the inside and the carry-out port 15b, respectively. .
The cooler 17 can cool the inside of the predetermined space 15c surrounded by the ceiling surface and side surfaces of the cooling tunnel structure 15 and the sheet 16 to a desired cool air state, and can usually control the cooling temperature. Part. The cooler 17 is preferably an apparatus having a cooling capacity capable of maintaining the inside of the predetermined space 15c at about +5 to −10 ° C.
In the humidification / cooling device 10 shown in FIG. 1, the humidifying tunnel structure 12 and the cooling tunnel structure 15 are arranged separately on the belt conveyor 11, and the distance of the separation can be selected as appropriate, It is also possible to place them in contact without being separated.
Next, the operation of the humidifying / cooling device 10 shown in FIG. 1 will be described.
In the production method of the present invention, the molded product 18 obtained by carrying out the above steps (A) to (D) is transported on the belt conveyor 11 of the humidification / cooling device 10, and is first preliminarily used by the humidifier 14. It passes through the inlet 12a of the humidifying tunnel structure 12 maintained in a desired moisture state, passes through the structure 12, and is carried out from the outlet 12b. At this time, by adjusting the speed of the belt conveyor 11 and the length of the humidifying tunnel structure 12 and adjusting the passage time of the molded article 18 passing through the structure 12, the surface layer of the molded article 18 is set to a predetermined level. It can be a layer of neutral salt.
Then, the humidified molded article 18 passes through the inlet 15a and the sheet 16 of the cooling tunnel structure 15 and proceeds into the predetermined space 15c. The inside of the predetermined space 15c is previously held at a desired temperature of 5 ° C. or less by the cooler 17. When the molded product 18 passes through the sheet 16, the predetermined space 15c temporarily becomes an open system. However, after the passage, the sheet 16 is restored and the space 15c is substantially returned to the closed system. Is efficiently maintained at a desired cooling temperature state. By adjusting the speed of the belt conveyor 11 and the length of the predetermined space 15c, and adjusting the passage time of the molded product 18 passing through the predetermined space 15c, the surface layer of the molded product 18 is brought into a desired cooling and drying state, The surface hardness of the molded product 18 can be improved efficiently.
The molded product 18 having improved surface hardness passes through the sheet 16 on the carry-out port 15 b side and the carry-out port 15 b and is carried out of the cooling tunnel structure 15.
In the humidification / cooling device 10 of the present invention, a shrink device and / or packaging device for the molded product 18 can be installed behind the cooling tunnel structure 15 as desired.

以下、実施例により、本発明を更に詳細に説明するが、本発明はこれらに限定されない。
なお、各実施例において成形物を通過させる加湿室及び冷却室としては、図1に示す加湿・冷却装置10を用いた。
EXAMPLES Hereinafter, although an Example demonstrates this invention further in detail, this invention is not limited to these.
In each example, the humidification / cooling device 10 shown in FIG. 1 was used as the humidification chamber and the cooling chamber through which the molded product passes.

平均分子量500のPEG6.7重量部及び平均分子量3700のPEG6.7重量部を、温度60℃でジプロピレングリコール6.7重量部に溶解し、平均分子量2100のPEG溶液を調製した。次いで、クエン酸27.2重量部、炭酸ナトリウム27.2重量部、無水硫酸ナトリウム25.3重量部、色素0.1重量部及び香料0.1重量部に、前記PEG溶液を混合撹拌し、湿潤粉末原料を調製した。
得られた湿潤粉末原料とプラスチック製の玩具とを加圧成形機の容器に入れ、圧力3kgf/cmで加圧してタマゴ型に成形した後、成形物を加圧成形機の容器から取出した。次に、ベルトコンベア上に、超音波加湿器により霧状水雰囲気とした加湿室と、−2〜−5℃に制御された冷却室とを直列に配置した装置を用意し、該ベルトコンベア上に前記取出した成形物を載置し、加湿室及び冷却室を通過させることにより有形物含有固体入浴剤を製造した。この際、加湿室の通過時間を1分間、冷却室の通過時間を6分間とした。
得られた固体入浴剤は、加湿室及び冷却室を通過する前の成形物に比して格段に表面硬度が向上しており、また、表面が中性塩層で覆われていた。
次いで、得られた固体入浴剤を常法によりシュリンク処理した後、細孔を有するアルミ箔製の袋に入れ、常温で1ヶ月間保存した。1ヶ月後に袋を開封し、製造時の臭い及び色と比較した結果、ほとんど変化は認められなかった。また、この固体入浴剤を浴湯に投入したところ、浴湯中に沈み、炭酸ガスの発泡が数分間持続した後、玩具が浴湯面に浮上した。この玩具に変形は認められなかった。
6.7 parts by weight of PEG having an average molecular weight of 500 and 6.7 parts by weight of PEG having an average molecular weight of 3700 were dissolved in 6.7 parts by weight of dipropylene glycol at a temperature of 60 ° C. to prepare a PEG solution having an average molecular weight of 2100. Next, 27.2 parts by weight of citric acid, 27.2 parts by weight of sodium carbonate, 25.3 parts by weight of anhydrous sodium sulfate, 0.1 part by weight of pigment and 0.1 part by weight of fragrance are mixed and stirred, A wet powder material was prepared.
The obtained wet powder raw material and plastic toy were put in a container of a pressure molding machine, pressed at a pressure of 3 kgf / cm 2 and molded into an egg mold, and the molded product was taken out from the container of the pressure molding machine. . Next, on the belt conveyor, a device is prepared in which a humidifying chamber made into a mist water atmosphere by an ultrasonic humidifier and a cooling chamber controlled at −2 to −5 ° C. are arranged in series. The molded product thus taken out was placed and passed through a humidifying chamber and a cooling chamber to produce a solid bath containing tangible material. At this time, the passage time in the humidification chamber was 1 minute, and the passage time in the cooling chamber was 6 minutes.
The obtained solid bath agent had a markedly improved surface hardness as compared with the molded product before passing through the humidification chamber and the cooling chamber, and the surface was covered with a neutral salt layer.
Next, the obtained solid bath agent was subjected to a shrink treatment by a conventional method, and then placed in a bag made of aluminum foil having pores and stored at room temperature for one month. After 1 month, the bag was opened and compared with the odor and color at the time of manufacture. As a result, almost no change was observed. Moreover, when this solid bath was poured into the bath water, it submerged in the bath water, and after the foaming of carbon dioxide gas continued for several minutes, the toy surfaced on the bath water surface. No deformation was found in this toy.

平均分子量500のPEG9.5重量部及び平均分子量3700のPEG9.5重量部を、温度60℃でジプロピレングリコール1.1重量部に溶解し、平均分子量2100のPEG溶液を調製した。次いで、コハク酸27.2重量部、炭酸水素ナトリウム27.2重量部、無水硫酸ナトリウム25.3重量部、色素0.1重量部及び香料0.1重量部に、前記PEG溶液を混合撹拌し、湿潤粉末原料を調製した。
得られた湿潤粉末原料とプラスチック製の玩具とを加圧成形機の容器に入れ、圧力を4kgf/cmに代えた以外は実施例1と同様にタマゴ型成形物を得、次いで、実施例1と同様に加室、冷却を行って有形物含有固体入浴剤を製造した。
得られた固体入浴剤は、加湿室及び冷却室を通過する前の成形物に比して格段に表面硬度が向上しており、また、表面が中性塩層で覆われていた。
次いで、得られた固体入浴剤を常法によりシュリンク処理した後、細孔を有するアルミ箔製の袋に入れ、常温で3ヶ月間保存した。3ヶ月後に袋を開封し、製造時の臭い及び色と比較した結果、ほとんど変化は認められなかった。また、この固体入浴剤を浴湯に投入したところ、浴湯中に沈み、炭酸ガスの発泡が数分間持続した後、玩具が浴湯面に浮上した。この玩具に変形は認められなかった。水溶性湿潤粉末の入浴剤原料を調製した。
9.5 parts by weight of PEG having an average molecular weight of 500 and 9.5 parts by weight of PEG having an average molecular weight of 3700 were dissolved in 1.1 parts by weight of dipropylene glycol at a temperature of 60 ° C. to prepare a PEG solution having an average molecular weight of 2100. Next, 27.2 parts by weight of succinic acid, 27.2 parts by weight of sodium hydrogen carbonate, 25.3 parts by weight of anhydrous sodium sulfate, 0.1 part by weight of dye and 0.1 part by weight of fragrance were mixed and stirred. A wet powder raw material was prepared.
The egg-shaped molded product was obtained in the same manner as in Example 1 except that the obtained wet powder raw material and plastic toy were placed in a container of a pressure molding machine and the pressure was changed to 4 kgf / cm 2. The tangible-containing solid bathing agent was produced by performing chambering and cooling in the same manner as in 1.
The obtained solid bath agent had a markedly improved surface hardness as compared with the molded product before passing through the humidification chamber and the cooling chamber, and the surface was covered with a neutral salt layer.
Next, the obtained solid bath agent was subjected to a shrink treatment by a conventional method, and then placed in a bag made of aluminum foil having pores and stored at room temperature for 3 months. As a result of opening the bag after 3 months and comparing it with the odor and color at the time of manufacture, almost no change was observed. Moreover, when this solid bath was poured into the bath water, it submerged in the bath water, and after the foaming of carbon dioxide gas continued for several minutes, the toy surfaced on the bath water surface. No deformation was found in this toy. A water-soluble wet powder bath agent raw material was prepared.

平均分子量500のPEG10.0重量部を、温度60℃でジプロピレングリコール10.1重量部に溶解しPEG溶液を調製した。次いで、クエン酸13.6重量部、コハク酸13.6重量部、炭酸水素ナトリウム26.2重量部、無水硫酸ナトリウム26.3重量部、色素0.1重量部及び香料0.1重量部に、前記PEG溶液を混合撹拌し、湿潤粉末原料を調製した。
得られた湿潤粉末原料とプラスチック製の玩具とを加圧成形機の容器に入れ、圧力を1.3kgf/cmに代えた以外は実施例1と同様にタマゴ型成形物を得、次いで、実施例1と同様に加室、冷却を行って有形物含有固体入浴剤を製造した。
得られた固体入浴剤は、加湿室及び冷却室を通過する前の成形物に比して格段に表面硬度が向上しており、また、表面が中性塩層で覆われていた。
次いで、得られた固体入浴剤を常法によりシュリンク処理した後、細孔を有するアルミ箔製の袋に入れ、常温で6ヶ月間保存した。6ヶ月後に袋を開封し、製造時の臭い及び色と比較した結果、ほとんど変化は認められなかった。また、この固体入浴剤を浴湯に投入したところ、浴湯中に沈み、炭酸ガスの発泡が数分間持続した後、玩具が浴湯面に浮上した。この玩具に変形は認められなかった。水溶性湿潤粉末の入浴剤原料を調製した。
10.0 parts by weight of PEG having an average molecular weight of 500 was dissolved in 10.1 parts by weight of dipropylene glycol at a temperature of 60 ° C. to prepare a PEG solution. Next, 13.6 parts by weight of citric acid, 13.6 parts by weight of succinic acid, 26.2 parts by weight of sodium hydrogen carbonate, 26.3 parts by weight of anhydrous sodium sulfate, 0.1 part by weight of pigment and 0.1 part by weight of fragrance The PEG solution was mixed and stirred to prepare a wet powder material.
The obtained wet powder raw material and plastic toy were put in a container of a pressure molding machine, and an egg-shaped molded product was obtained in the same manner as in Example 1 except that the pressure was changed to 1.3 kgf / cm 2 . In the same manner as in Example 1, chambering and cooling were performed to produce a tangible material-containing solid bath.
The obtained solid bath agent had a markedly improved surface hardness as compared with the molded product before passing through the humidification chamber and the cooling chamber, and the surface was covered with a neutral salt layer.
Next, the obtained solid bath agent was subjected to a shrink treatment by a conventional method, and then placed in a bag made of aluminum foil having pores and stored at room temperature for 6 months. After 6 months, the bag was opened and compared with the odor and color at the time of manufacture. As a result, almost no change was observed. Moreover, when this solid bath was poured into the bath water, it submerged in the bath water, and after the foaming of carbon dioxide gas continued for several minutes, the toy surfaced on the bath water surface. No deformation was found in this toy. A water-soluble wet powder bath agent raw material was prepared.

平均分子量500のPEG7.7重量部及び平均分子量3700のPEG7.7重量部を、温度60℃でジプロピレングリコール4.7重量部に溶解し、平均分子量2100のPEG溶液を調製した。次いで、酒石酸27.2重量部、炭酸ナトリウム27.2重量部、無水硫酸ナトリウム25.3重量部、色素0.1重量部及び香料0.1重量部に、前記PEG溶液を混合撹拌し、湿潤粉末原料を調製した。
得られた湿潤粉末原料とプラスチック製の玩具とを加圧成形機の容器に入れ、圧力を1.5kgf/cmに代えた以外は実施例1と同様にタマゴ型成形物を得、次いで、実施例1と同様に加室、冷却を行って有形物含有固体入浴剤を製造した。
得られた固体入浴剤は、加湿室及び冷却室を通過する前の成形物に比して格段に表面硬度が向上しており、また、表面が中性塩層で覆われていた。
次いで、得られた固体入浴剤を常法によりシュリンク処理した後、細孔を有するアルミ箔製の袋に入れ、常温で6ヶ月間保存した。6ヶ月後に袋を開封し、製造時の臭い及び色と比較した結果、ほとんど変化は認められなかった。また、この固体入浴剤を浴湯に投入したところ、浴湯中に沈み、炭酸ガスの発泡が数分間持続した後、玩具が浴湯面に浮上した。この玩具に変形は認められなかった。
7.7 parts by weight of PEG having an average molecular weight of 500 and 7.7 parts by weight of PEG having an average molecular weight of 3700 were dissolved in 4.7 parts by weight of dipropylene glycol at a temperature of 60 ° C. to prepare a PEG solution having an average molecular weight of 2100. Next, 27.2 parts by weight of tartaric acid, 27.2 parts by weight of sodium carbonate, 25.3 parts by weight of anhydrous sodium sulfate, 0.1 part by weight of the dye and 0.1 part by weight of the fragrance were mixed and stirred, and wetted. A powder raw material was prepared.
The obtained wet powder raw material and plastic toy were put into a container of a pressure molding machine, and an egg shaped molded product was obtained in the same manner as in Example 1 except that the pressure was changed to 1.5 kgf / cm 2 . In the same manner as in Example 1, chambering and cooling were performed to produce a tangible material-containing solid bath.
The obtained solid bath agent had a markedly improved surface hardness as compared with the molded product before passing through the humidification chamber and the cooling chamber, and the surface was covered with a neutral salt layer.
Next, the obtained solid bath agent was subjected to a shrink treatment by a conventional method, and then placed in a bag made of aluminum foil having pores and stored at room temperature for 6 months. After 6 months, the bag was opened and compared with the odor and color at the time of manufacture. As a result, almost no change was observed. Moreover, when this solid bath was poured into the bath water, it submerged in the bath water, and after the foaming of carbon dioxide gas continued for several minutes, the toy surfaced on the bath water surface. No deformation was found in this toy.

Claims (8)

発泡性成分としての有機酸及び炭酸塩を含む粉末原料、及び結着性液状物を混合して得た湿潤粉末原料を準備する工程(A)と、
所定圧力により変形しうる水不溶性の有形物、及び工程(A)で準備した湿潤粉末原料を、加圧成形するための容器内に、該有形物が湿潤粉末原料に内包されるように入れる工程(B)と、
工程(B)において容器内に収容された有形物及び湿潤粉末原料を、所定形状の型を用いて0.5〜10kf/cmの圧力により加圧成形する工程(C)と、
工程(C)により加圧成形された成形物を前記容器内から取出す工程(D)と、
得られた成形物の表面層を加湿する工程(E)と、
工程(E)に続いて成形物を5℃以下に冷却する工程(F)とを含む有形物含有固体入浴剤の製造法。
A step of preparing a powder raw material containing an organic acid and a carbonate as a foamable component, and a wet powder raw material obtained by mixing a binding liquid;
A step of placing a water-insoluble tangible material that can be deformed by a predetermined pressure and the wet powder raw material prepared in step (A) into a container for pressure molding so that the tangible material is included in the wet powder raw material. (B) and
A step (C) of pressure-molding the tangible material and wet powder raw material contained in the container in the step (B) with a pressure of 0.5 to 10 kf / cm 2 using a mold having a predetermined shape;
A step (D) of taking out the molded product pressure-molded in the step (C) from the container;
A step (E) of humidifying the surface layer of the obtained molded product;
A process for producing a tangible material-containing solid bath containing a step (E) followed by a step (F) of cooling the molded product to 5 ° C. or lower.
工程(A)に用いる粉末原料が、無水硫酸ナトリウムを含み、得られる固体入浴剤の比重が浴湯の比重より高くなるように該無水硫酸ナトリウムの配合割合を調整する請求の範囲1の製造法。The process according to claim 1, wherein the powder raw material used in the step (A) contains anhydrous sodium sulfate, and the blending ratio of the anhydrous sodium sulfate is adjusted so that the specific gravity of the obtained solid bath agent is higher than the specific gravity of the bath water. . 工程(E)の加湿を、超音波加湿器を用いて行う請求の範囲1の製造法。The manufacturing method according to claim 1, wherein the humidification in the step (E) is performed using an ultrasonic humidifier. 工程(F)の冷却を、+5〜−10℃において、1〜30分間行う請求の範囲1の製造法。The manufacturing method according to claim 1, wherein the cooling in the step (F) is performed at +5 to -10 ° C for 1 to 30 minutes. 請求の範囲1の製造法に用いる加湿・冷却装置であって、加圧成形された成形物をライン上で搬送する搬送手段と、前記成形物を加湿する加湿手段と、前記成形物を冷却する冷却手段とを備え、
前記加湿手段が、成形物の搬入口及び搬出口を有する加湿トンネル構造体と、該加湿トンネル構造体内を加湿しうる加湿器とを備え、
前記冷却手段が、成形物の搬入口及び搬出口を有する冷却トンネル構造体と、該冷却トンネル構造体内の所定空間を冷却しうる冷却器とを備え、前記冷却トンネル構造体が、前記冷却器により冷却する所定空間内の冷気を保持し、且つ成形物の通過を可能にした可撓性の冷気遮蔽手段を、前記搬入口側及び搬出口側に各々少なくとも1つずつ有し、
前記加湿手段と前記冷却手段とを、前記搬送手段のライン上にこの順に配置した加湿・冷却装置。
A humidifying / cooling device used in the manufacturing method according to claim 1, wherein a conveying means for conveying a pressure-formed molded article on a line, a humidifying means for humidifying the molded article, and the molded article are cooled. Cooling means,
The humidifying means comprises a humidifying tunnel structure having a carry-in port and a carry-out port for a molded article, and a humidifier capable of humidifying the humidifying tunnel structure,
The cooling means comprises a cooling tunnel structure having a carry-in port and a carry-out port for a molded product, and a cooler capable of cooling a predetermined space in the cooling tunnel structure, and the cooling tunnel structure is formed by the cooler. Having at least one flexible cold air shielding means for holding the cold air in a predetermined space to be cooled and allowing the molded product to pass therethrough on each of the carry-in side and the carry-out side;
A humidifying / cooling device in which the humidifying means and the cooling means are arranged in this order on a line of the conveying means.
前記加湿器が、超音波加湿器である請求の範囲5の加湿・冷却装置。The humidifying / cooling device according to claim 5, wherein the humidifier is an ultrasonic humidifier. 前記冷却トンネル構造体が、前記冷気遮蔽手段を、前記搬入口側及び搬出口側に各々複数有する請求の範囲5の加湿・冷却装置。The humidification / cooling device according to claim 5, wherein the cooling tunnel structure has a plurality of the cold air shielding means on each of the carry-in port side and the carry-out port side. 前記冷気遮断手段が、冷却トンネル構造体の天井面から吊り下げられた、下方から上方に複数のスリットを設けた可撓性のプラスチック製シートである請求の範囲5の加湿・冷却装置。6. The humidifying / cooling device according to claim 5, wherein the cold air blocking means is a flexible plastic sheet suspended from the ceiling surface of the cooling tunnel structure and provided with a plurality of slits from below to above.
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