JPH10203965A - Production of covered preparation - Google Patents

Production of covered preparation

Info

Publication number
JPH10203965A
JPH10203965A JP9013702A JP1370297A JPH10203965A JP H10203965 A JPH10203965 A JP H10203965A JP 9013702 A JP9013702 A JP 9013702A JP 1370297 A JP1370297 A JP 1370297A JP H10203965 A JPH10203965 A JP H10203965A
Authority
JP
Japan
Prior art keywords
coating
substance
coated
core
preparation
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
JP9013702A
Other languages
Japanese (ja)
Inventor
Masaru Miyawaki
勝 宮脇
Seiichi Kodama
成一 児玉
Kenji Nakamura
健二 中村
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.)
Takeda Pharmaceutical Co Ltd
Original Assignee
Takeda Chemical Industries 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 Takeda Chemical Industries Ltd filed Critical Takeda Chemical Industries Ltd
Priority to JP9013702A priority Critical patent/JPH10203965A/en
Publication of JPH10203965A publication Critical patent/JPH10203965A/en
Pending legal-status Critical Current

Links

Abstract

PROBLEM TO BE SOLVED: To provide a simple method for producing a covered preparation of hydrophilic material such as L-ascorbic acid and other organic acids, having sufficient coverage. SOLUTION: This method for producing a covered preparation by covering the periphery of a hydrophilic core material with plural layers of a hydrophobic and thermally melting covering material comprises successively or separately adding the heated and melted covering material to the core material while stirring the core material at a temperature lower than a solidifying temperature of the covering material and solidifying the molten covering material to form plural covering material layers around the periphery of the core material.

Description

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

【0001】[0001]

【発明が属する技術分野】本発明は、被覆製剤の製造
法、さらに詳しくは、有用な親水性物質、特に、有機酸
やその塩のような有機物質を芯とし、該芯物質の表面を
複数の層の疎水性物質で被覆した、芯物質への外部から
の影響またはその外部への影響を少なくして、芯物質の
物性を改良した安定な被覆製剤の製造法に関する。
[0001] The present invention relates to a method for producing a coated preparation, and more particularly, to a method in which a useful hydrophilic substance, in particular, an organic substance such as an organic acid or a salt thereof is used as a core, and the surface of the core substance is formed by a plurality of methods. The present invention relates to a method for producing a stable coated preparation in which physical properties of the core substance are improved by reducing the external influence or the external influence on the core substance by coating the layer with a hydrophobic substance.

【0002】[0002]

【従来の技術】クエン酸、フマル酸、ソルビン酸等の有
機酸は、酸味料として、pH調整剤として、保存目的と
しての利用等に広く使用されているが、食品等の加工中
や保存中に、低pHによる悪影響がみられることが多
い。また、L−アスコルビン酸は、品質改良剤としての
利用、酸味料としての利用、ビタミンCとしての栄養強
化剤における利用、医薬としての利用等各種の食品、健
康食品、飼料、医薬品分野等に広く使用されている。L
−アスコルビン酸の品質改良剤としての利用は、反応性
を期待した酸化・還元能を有効に利用した用途である
が、反応速度が速すぎて効果が長期間持続しない欠点を
有している。一方、強化剤としての利用においては、食
品等の加工、保存中では安定に保持されていることが望
ましいが、水、酸素、金属塩等が共存する系では、安定
に保持することが難しく、期待される機能が発揮されな
いばかりでなく、場合によっては、酸化・還元反応によ
り他の成分へ悪影響する欠点も有している。そこで、こ
のような問題点を解決する方法の1つとして、従来、こ
れらの有機酸を、芯とし、その表面を疎水性の物質で被
覆する方法、例えば、有機酸の微粉を、常温で固体で熱
溶融性の油脂等の被覆物質により、噴霧冷却法、スプレ
ーコーティング法や、回転混合し、乾燥する方法等によ
り包み、水や酸素等との接触を防ぎ、反応性を制御する
方法が提案されている。
2. Description of the Related Art Organic acids such as citric acid, fumaric acid and sorbic acid are widely used as sour agents, pH regulators, and for storage purposes. In addition, adverse effects due to low pH are often observed. In addition, L-ascorbic acid is widely used in various foods, health foods, feeds, pharmaceuticals, etc., such as use as a quality improving agent, use as a sour agent, use as a nutrient enhancer as vitamin C, use as a medicine, and the like. It is used. L
-The use of ascorbic acid as a quality improving agent is an application that effectively utilizes the oxidation / reduction ability in expectation of reactivity, but has a disadvantage that the reaction rate is too fast and the effect does not last for a long time. On the other hand, in the use as a fortifying agent, it is desirable that food and the like are stably maintained during processing and storage, but in a system where water, oxygen, metal salts, and the like coexist, it is difficult to stably maintain the system. Not only does the expected function not be exerted, but also in some cases, it has the disadvantage of adversely affecting other components due to oxidation and reduction reactions. Therefore, as one method of solving such a problem, conventionally, a method in which these organic acids are used as a core and the surface thereof is coated with a hydrophobic substance, for example, a fine powder of an organic acid is solidified at room temperature. A method to control the reactivity by preventing the contact with water, oxygen, etc. by wrapping it with a spray cooling method, a spray coating method, a method of spin-mixing and drying, etc., using a coating material such as a hot-melt oil or fat Have been.

【0003】[0003]

【発明が解決しようとする課題】このような方法として
は、水溶性ビタミン類や有機酸の粉末のごとき芯物質
に、被覆物質の油脂類を、接触・衝突させ、被覆物質を
芯物質に付着・被覆させて被覆製剤を得る方法(特開昭
63−164863号、特開昭63−164864号、
特開昭63−258813号)、微粒の有機酸と溶融油
脂類を、高温下で混合し、噴霧冷却して微粉の製剤を得
る方法(特開昭55−92661号、特開昭62−18
152号、特開昭64−3118号、特開昭64−31
19号)、油脂類を溶媒に溶解し、流動層装置により溶
媒を飛散させながら有機酸の表面に被覆する方法(特開
昭50−52221号)等が提案されているが、芯物質
の粒子径が制限される、被覆度が十分でない、高油脂被
覆品が製造できない、作業性が悪い、特別な装置が必
要、単核粒子品の製造に向かない、大量生産に向かな
い、高価格等の問題がある。本発明は、かかる問題を改
善することを目的とする。
As such a method, oils and fats as a coating substance are brought into contact with and impinged on a core substance such as a powder of water-soluble vitamins or organic acids, and the coating substance is attached to the core substance. A method of obtaining a coated preparation by coating (JP-A-63-164863, JP-A-63-164864,
JP-A-63-258813), a method of mixing finely divided organic acids and molten fats and oils at a high temperature and spray cooling to obtain a fine powder formulation (JP-A-55-92661, JP-A-62-18).
No. 152, JP-A-64-3118, JP-A-64-31
No. 19), a method of dissolving fats and oils in a solvent and coating the surface of the organic acid while scattering the solvent with a fluidized bed apparatus (Japanese Patent Laid-Open No. 50-52221). Limited diameter, insufficient coverage, inability to manufacture high oil / fat coated products, poor workability, special equipment required, not suitable for manufacturing mononuclear particle products, not suitable for mass production, high price, etc. There is a problem. An object of the present invention is to improve such a problem.

【0004】[0004]

【課題を解決するための手段】本発明者らの検討によれ
ば、上記の従来の方法における問題は、均一で厚い被覆
が容易にできないこと、また、製造の困難さから、芯物
質としての有機酸等の反応性や、被覆製剤からの溶出速
度の制御が困難であることにより発生する。そこで、本
発明者らは、簡単な製造法で、自由に反応性や溶出速度
の制御が可能な被覆製剤の開発をめざして鋭意検討し
た。その結果、撹拌混合機中で温度調整したL−アスコ
ルビン酸に、加熱溶融した油脂類および/ワックス類を
連続的または分割して添加し、添加・固化を繰り返して
芯物質の表面に油脂類を被覆すると、複数の、高油脂量
の、厚い被覆層の、単核粒子の油脂被覆製剤ができ、こ
れが他の親水性の芯物質にも適用できることを見いだ
し、本発明を完成するに至った。
According to the study of the present inventors, the problems in the above-mentioned conventional method are that the uniform and thick coating cannot be easily formed, and the difficulty in the production makes it difficult to use the core material as a core material. It is caused by difficulty in controlling the reactivity of organic acids and the like and the dissolution rate from the coated preparation. Therefore, the present inventors have intensively studied to develop a coated preparation capable of freely controlling the reactivity and the dissolution rate by a simple production method. As a result, the fats and oils and / or waxes heated and melted are continuously or dividedly added to the L-ascorbic acid whose temperature has been adjusted in the stirring mixer, and the addition and solidification are repeated to deposit the fats and oils on the surface of the core material. When coated, a plurality of fat-coated preparations with a high fat content, a thick coating layer and mononuclear particles were formed, and it was found that this preparation could be applied to other hydrophilic core substances, and the present invention was completed.

【0005】すなわち、本発明は、親水性の芯物質の周
囲を複数の層の疎水性熱溶融性の被覆物質で被覆した製
剤の製造に際し、芯物質を、被覆物質の固化温度以下の
温度で混合しながら、加熱溶融した被覆物質を連続的ま
たは分割して添加しつつ、固化させ、芯物質の周囲に複
数の被覆物質層を形成させることを特徴とする被覆製剤
の製造法を提供するものである。本発明によれば、被覆
物質や、その被覆量、すなわち、被覆物質の層の数、添
加速度を適宜選択し、適正に温度制御することにより、
水溶出性の制御された、かつ外部からの酸素、酵素、金
属等の影響あるいは外部への影響の制御された安定性の
優れた親水性芯物質の被覆製剤が簡便に得られる。
That is, the present invention relates to a method for producing a preparation in which a hydrophilic core material is coated with a plurality of layers of a hydrophobic heat-meltable coating material, the core material is treated at a temperature lower than the solidification temperature of the coating material. A method for producing a coated preparation characterized by solidifying while adding a coating substance heated and melted continuously or dividedly while mixing to form a plurality of coating substance layers around a core substance. It is. According to the present invention, the coating material and its coating amount, that is, the number of layers of the coating material, the addition rate is appropriately selected, by appropriately controlling the temperature,
It is possible to easily obtain a coated preparation of a hydrophilic core substance having excellent stability with controlled water elution property and controlled by the influence of external oxygen, enzymes, metals and the like or the external influence.

【0006】[0006]

【発明の実施の形態】本発明においては、芯物質は、適
宜の粒径を有する親水性の物質であれば、特に限定する
ものではなく、例えば、クエン酸、フマル酸、酒石酸、
ソルビン酸、L−アスコルビン酸、ニコチン酸、パント
テン酸のような水溶性ビタミン類、アミノ酸類、核酸類
またはそれらのアルカリ金属塩(例、カリウム塩、ナト
リウム塩等)、アルカリ土類金属塩(例、カルシウム
塩、マグネシウム塩等)の親水性の有機酸および有機酸
塩類、ビタミンB群のごとき水溶性の非有機酸系ビタミ
ン類およびグルコース、シュークロース等の糖類が挙げ
られる。これらは、通常、平均粒径2000μm以下、
好ましくは40〜1000μmの、粉末状、造粒品また
は結晶状で使用される。
DESCRIPTION OF THE PREFERRED EMBODIMENTS In the present invention, the core substance is not particularly limited as long as it is a hydrophilic substance having an appropriate particle size. For example, citric acid, fumaric acid, tartaric acid,
Water-soluble vitamins such as sorbic acid, L-ascorbic acid, nicotinic acid, pantothenic acid, amino acids, nucleic acids or their alkali metal salts (eg, potassium salt, sodium salt, etc.), alkaline earth metal salts (eg, , Calcium salts, magnesium salts, etc.), water-soluble non-organic acid vitamins such as vitamin B group, and sugars such as glucose and sucrose. These usually have an average particle size of 2000 μm or less,
It is preferably used in the form of a powder, granulated product or crystal having a size of 40 to 1000 μm.

【0007】被覆物質としては、疎水性熱溶融性の物質
が使用され、かかる物質としては、融点が50〜90
℃、好ましくは約60〜80℃で食用に供し得るもので
あればよく、例えば、植物性および動物性油脂、それら
の水素添加、分別、エステル交換油脂、脂肪酸、脂肪酸
エステル類、植物性、動物性および鉱物性の天然ワック
ス類等が挙げられる。油脂類の具体例としては、例え
ば、大豆硬化油、牛脂硬化油、ナタネ硬化油、魚油硬化
油、鯨油硬化油、ヒマシ油硬化油、サフラワー油硬化
油、紅花油硬化油等が挙げられる。脂肪酸の具体例とし
ては、炭素数14〜28で、融点が約50〜90℃の脂
肪酸(例、パルミチン酸、ステアリン酸、ベヘン酸等)
および界面活性剤としての作用を有するこれらのグリセ
リンエステル、蔗糖エステル、ソルビトールエステル、
プロピレングリコールエステル等を用いることもでき
る。
As the coating substance, a hydrophobic heat-meltable substance is used, and as such a substance, the melting point is 50 to 90.
C., preferably about 60-80.degree. C., for example, vegetable and animal fats and oils, hydrogenation, fractionation, transesterification fats, fatty acids, fatty acid esters, vegetable and animals. And mineral natural waxes. Specific examples of fats and oils include, for example, hydrogenated soybean oil, hydrogenated beef tallow, hydrogenated rapeseed oil, hydrogenated fish oil, hydrogenated whale oil, hydrogenated castor oil, hydrogenated safflower oil, hydrogenated safflower oil, and the like. As a specific example of the fatty acid, a fatty acid having 14 to 28 carbon atoms and a melting point of about 50 to 90 ° C. (eg, palmitic acid, stearic acid, behenic acid, etc.)
Glycerin esters, sucrose esters, sorbitol esters, and glycerol esters having an action as a surfactant;
Propylene glycol esters and the like can also be used.

【0008】ワックス類の具体例としては、キャンデリ
ラワックス、ライスワックス、カルナウバワックス、ミ
ツロウ、パラフィンワックスなどの可食性天然ワックス
類が挙げられる。本発明においては、これらの被覆物質
は、単独で使用してもよいし、2種以上を組み合わせて
もよい。また、同じ被覆物質の層を複数形成させてもよ
く、被覆物質の組み合わせによっては、異なる被覆物質
の層を組み合わせて形成させることもできる。被覆物質
は、芯物質99〜1重量部、好ましくは95〜20重量
部、さらに好ましくは90〜40重量部に対し、1〜9
9重量部、好ましくは、5〜80重量部、さらに好まし
くは、10〜60重量部の割合で使用するのがよい。被
覆物質の量が少なすぎると、被覆が不十分となる。少な
くとも2層以上の被覆物質で被覆されるような被覆物質
の量を選択する。複数の被覆層を設けることにより、十
分な被覆度が得られ、高油脂量の厚い被覆層を有する単
核粒子の被覆製剤が得られる。
[0008] Specific examples of waxes include edible natural waxes such as candelilla wax, rice wax, carnauba wax, beeswax, and paraffin wax. In the present invention, these coating substances may be used alone or in combination of two or more. Further, a plurality of layers of the same coating substance may be formed, and depending on the combination of the coating substances, layers of different coating substances may be formed in combination. The coating material is used in an amount of 1 to 9 parts by weight based on 99 to 1 part by weight of the core substance, preferably 95 to 20 parts by weight, more preferably 90 to 40 parts by weight.
9 parts by weight, preferably 5 to 80 parts by weight, more preferably 10 to 60 parts by weight. If the amount of coating material is too small, the coating will be insufficient. The amount of coating material is selected such that it is coated with at least two or more coating materials. By providing a plurality of coating layers, a sufficient degree of coverage can be obtained, and a coated preparation of mononuclear particles having a thick coating layer with a high fat content can be obtained.

【0009】本発明の製造法は、温度調整が可能な撹拌
混合装置を用いて実施する。かかる装置としては、芯物
質と被覆物質を撹拌、混合できる装置であればよく、特
に限定するものでないが、温度調整が可能なスクリュー
型、リボン型、パドル型、高速流動型、回転円板型など
の撹拌混合機を使用することが操作の容易性、効率性か
ら好ましい。例えば、マイクロスピードミキサー(宝工
機)、ハイスピードミキサー(深江工業)、ナウターミ
キサー等の撹拌混合装置を使用できる。本発明の製造法
を実施するには、例えば、上記混合機を使用して芯物質
を被覆物質の固化温度以下の温度まで加熱昇温し、これ
に加熱溶融した被覆物質を連続的または分割して添加
し、粒子の結着を防ぎながら固化・添加を繰り返して芯
物質の表面に油脂等を均一に年輪状または渦巻き状に多
層被覆したのち冷却する。
[0009] The production method of the present invention is carried out using a stirring and mixing device capable of adjusting the temperature. Such a device may be any device that can stir and mix the core material and the coating material, and is not particularly limited, but a screw type, a ribbon type, a paddle type, a high-speed flow type, and a rotating disk type capable of adjusting the temperature. It is preferable to use a stirring mixer such as the above because of easiness of operation and efficiency. For example, a stirring and mixing device such as a micro speed mixer (Takara Kogyo), a high speed mixer (Fukae Kogyo), a Nauta mixer and the like can be used. In order to carry out the production method of the present invention, for example, the core material is heated to a temperature equal to or lower than the solidification temperature of the coating material by using the above mixer, and the coating material heated and melted is continuously or divided into the core material. After solidification and addition are repeated while preventing binding of particles, the surface of the core material is uniformly coated with oils and fats etc. in a multi-layered or spiral shape, and then cooled.

【0010】本発明の製造法は、特に、L−アスコルビ
ン酸の被覆製剤を製造するのに適しており、例えば、粒
子径が2000μm以下の粉末状、造粒品または結晶状
のL−アスコルビン酸100重量部を、被覆物質の固化
温度以下、例えば、40〜70℃に温度調整しながら混
合し、これに加熱溶融した被覆物質を連続的または分割
して1〜10000重量部加えて、添加、固化を繰り返
しすことにより、L−アスコルビン酸の表面に被覆物質
を多層被覆したL−アスコルビン酸被覆製剤が得られ
る。
The production method of the present invention is particularly suitable for producing a coated preparation of L-ascorbic acid. For example, powdered, granulated or crystalline L-ascorbic acid having a particle diameter of 2000 μm or less can be used. 100 parts by weight of the coating material is mixed at a temperature not higher than the solidification temperature of the coating material, for example, 40 to 70 ° C., and the heated and melted coating material is continuously or divided and added in an amount of 1 to 10000 parts by weight. By repeating the solidification, an L-ascorbic acid-coated preparation in which a coating substance is multi-layered on the surface of L-ascorbic acid is obtained.

【0011】かくして、本発明の製造法によれば、撹拌
混合装置のみの簡易な方法で親水性の芯物質を被覆する
ことができ、しかも、従来困難であった多層の、被覆層
の厚い、単核粒子を疎水性の被覆物質で被覆した製剤の
製造ができる利点を有している。得られた被覆製剤は、
医薬、食品、飼料等の分野において、芯物質の使用用途
に応じて、不安定な芯物質の安定化、芯物質の水溶出速
度、反応性の調整(徐放性)、芯物質の風味の放出制御
(酸味、臭味等の放出防止)等のために利用できる。例
えば、有機酸の低pHによる悪影響や、L−アスコルビ
ン酸の水、酸素、金属等による不安定化を防ぐことがで
き、逆に、L−アスコルビン酸の他の配合成分への影響
も防ぐことができる。また、チューインガム等における
呈味成分の徐放にも使用できる。
Thus, according to the production method of the present invention, a hydrophilic core substance can be coated by a simple method using only a stirring and mixing apparatus, and a multi-layer, thick coating layer, which has conventionally been difficult. There is an advantage that a preparation in which mononuclear particles are coated with a hydrophobic coating substance can be produced. The resulting coated formulation is
In the fields of medicine, food, feed, etc., depending on the intended use of the core substance, stabilization of the unstable core substance, water elution rate of the core substance, adjustment of reactivity (sustained release), flavor of the core substance It can be used for release control (prevention of release of acidity and odor). For example, it is possible to prevent the adverse effect of the low pH of the organic acid and the instability of L-ascorbic acid due to water, oxygen, metals and the like, and also to prevent the influence of L-ascorbic acid on other components. Can be. It can also be used for sustained release of taste components in chewing gum and the like.

【0012】[0012]

【実施例】以下に、実施例、比較例および使用例を挙げ
て本発明をさらに詳細に説明するが、本発明はこれらに
限定されるものではない。 実施例1 L−アスコルビン酸(平均粒子径350μm)500gを
ジャケット付き高速流動型混合機(ハイスピードミキサ
ーLSF−2型、深江工業製)に仕込み、撹拌しながら
60℃に加温し、温度を保持して撹拌を続けた。これ
に、撹拌下、別に用意した大豆硬化油(融点68℃)の
加熱溶融液100gを2分割して、一方の油脂50gを添
加して均一に被覆し、固化後に残り油脂50gを同方法
で添加して被覆した後、品温40℃まで冷却してL−ア
スコルビン酸の油脂被覆製剤を得た。 比較例1 溶融油脂を2分割しなかった以外は、実施例1の方法と
同方法で一度に溶融油脂を添加しL−アスコルビン酸の
油脂被覆製剤を得た。
The present invention will be described in more detail with reference to the following Examples, Comparative Examples and Use Examples, but the present invention is not limited thereto. Example 1 500 g of L-ascorbic acid (average particle size: 350 μm) was charged into a jacketed high-speed fluid mixer (high-speed mixer LSF-2, manufactured by Fukae Kogyo Co., Ltd.), and heated to 60 ° C. while stirring. Hold and continue stirring. Under stirring, 100 g of a heated melt of soy hardened oil (melting point 68 ° C.) prepared separately is divided into two portions, and 50 g of one of the fats and oils is added and uniformly coated. After the addition and coating, the product was cooled to a product temperature of 40 ° C. to obtain a fat-coated preparation of L-ascorbic acid. Comparative Example 1 The same procedure as in Example 1 was repeated except that the molten fat was not divided into two parts, to thereby obtain a L-ascorbic acid-coated preparation by adding the molten fat at once.

【0013】実施例1で得た油脂被覆製剤と比較例1で
得た油脂比較製剤の外観およびL−アスコルビン酸の水
溶出速度を比較した結果、比較例1の被覆品は、直径
0.5cm以上の固まりが多数発生して、細粒品はわずか
であったのに対して、実施例1の被覆品は固まりが少な
く、直径500μm以下の細粒品が約90%あった。ま
た、比較例1と実施例1の被覆品の細粒画分について、
L−アスコルビン酸の水溶出速度を比較したところ、比
較品は、約2分間程度で溶出したのに対して、実施例の
被覆品は約40分であり、顕著な被覆効果であった。す
なわち、比較例1のように、同時に添加すると、単核粒
子にならず、多量被覆ができず、また、溶出速度を遅延
させることができない。
As a result of comparing the appearance of the oil / fat coated preparation obtained in Example 1 and the oil / fat comparative preparation obtained in Comparative Example 1 and the water elution rate of L-ascorbic acid, the coated product of Comparative Example 1 was 0.5 cm in diameter. A large number of the above aggregates occurred, and the number of fine-grained products was slight, whereas the coated product of Example 1 had a small amount of clumps and about 90% of the fine-grained products having a diameter of 500 μm or less. Further, regarding the fine-grain fraction of the coated articles of Comparative Example 1 and Example 1,
When the water elution rate of L-ascorbic acid was compared, the comparative product eluted in about 2 minutes, whereas the coated product of the example was about 40 minutes, which was a remarkable coating effect. That is, as in Comparative Example 1, when they are added simultaneously, they do not become mononuclear particles, cannot be coated in a large amount, and cannot delay the dissolution rate.

【0014】実施例2 L−アスコルビン酸(平均粒子径120μm)500gを
ジャケット付き高速流動型混合機(ハイスピードミキサ
ーLSF−2型、深江工業製)に仕込み、撹拌しながら
50℃に加温し、撹拌を続けた。これに、撹拌下、別に
用意した大豆硬化油(融点68℃)の加熱溶融液200
gを、10g/分の速度で連続的に添加し均一に被覆した
のち、品温40℃まで冷却してL−アスコルビン酸の油
脂被覆製剤を得た。本品は、ほとんど固まりがなく、平
均粒子径は155μmの細粒品であった。
Example 2 500 g of L-ascorbic acid (average particle size: 120 μm) was charged into a jacketed high-speed fluid mixer (high-speed mixer LSF-2, manufactured by Fukae Kogyo) and heated to 50 ° C. with stirring. Stirring was continued. Then, under stirring, a heated melt 200 of hardened soybean oil (melting point 68 ° C) prepared separately was added.
g was continuously added at a rate of 10 g / min and uniformly coated, and then cooled to a product temperature of 40 ° C. to obtain an L-ascorbic acid-coated preparation. This product was hardly agglomerated and was a fine-grained product having an average particle size of 155 μm.

【0015】実施例3 L−アスコルビン酸(平均粒子径350μm)10kgを
ジャケット付き高速流動型混合機(マイクロスピードミ
キサーMS25型、宝工機製)に仕込み、撹拌しながら
50℃に加温し、撹拌を続けた。これに、撹拌下、別に
用意したナタネ硬化油(融点68℃)の加熱溶融液5kg
を、300g/分の速度で連続的に添加し均一に被覆し
たのち、品温40℃まで冷却してL−アスコルビン酸の
油脂被覆製剤を得た。
Example 3 10 kg of L-ascorbic acid (average particle diameter 350 μm) was charged into a jacketed high-speed flow mixer (Microspeed mixer MS25, manufactured by Takara Koki), heated to 50 ° C. while stirring, and stirred. Continued. 5 kg of a heated melt of rapeseed oil (melting point 68 ° C) prepared under stirring
Was added continuously at a rate of 300 g / min to coat uniformly, and then cooled to a product temperature of 40 ° C. to obtain a fat-coated formulation of L-ascorbic acid.

【0016】実施例4 L−アスコルビン酸(平均粒子径350μm)500gお
よび大豆硬化油50gをジャケット付き高速流動型混合
機(ハイスピードミキサーLSF−2型、深江工業製)
に仕込み、撹拌しながら70℃に加温して大豆硬化油を
溶融させた後、撹拌を続けた。これを、撹拌下、50℃
に冷却して固化させ(1次被覆)、つぎに大豆硬化油5
0gとグリセリン脂肪酸エステル(エマルジーMS、理
研ビタミン)10gの混合溶融品を加えて固化させ(2
次被覆)た後、20℃で冷却してL−アスコルビン酸の
2層油脂被覆製剤を得た。
Example 4 500 g of L-ascorbic acid (average particle size: 350 μm) and 50 g of hardened soybean oil were mixed with a high-speed fluidized mixer equipped with a jacket (high-speed mixer LSF-2, manufactured by Fukae Kogyo).
The mixture was heated to 70 ° C. while stirring to melt the hardened soybean oil, and then stirring was continued. This is stirred at 50 ° C.
And solidify (primary coating), then harden soybean oil 5
A mixed melt of 0 g and 10 g of glycerin fatty acid ester (Emulgy MS, RIKEN Vitamin) is added and solidified (2
Then, the mixture was cooled at 20 ° C. to obtain a two-layer oil-fat coating formulation of L-ascorbic acid.

【0017】実施例5 無水クエン酸(平均粒子径550μm)500gをジャケ
ット付き高速流動型混合機(ハイスピードミキサーLS
F−2型、深江工業製)に仕込み、撹拌しながら60℃
に加温し、撹拌を続けた。これに、撹拌下、別に用意し
た大豆硬化油(融点68℃)の加熱溶融液500gを、
3g/分の速度で連続的に添加し均一に被覆したのち、
品温40℃まで冷却してクエン酸の油脂被覆製剤を得
た。
Example 5 500 g of anhydrous citric acid (average particle size of 550 μm) was mixed with a jacketed high-speed fluid mixer (High Speed Mixer LS).
F-2 type, manufactured by Fukae Kogyo Co., Ltd.)
And continued stirring. To this, while stirring, 500 g of a heated melt of separately prepared soybean hardened oil (melting point 68 ° C.)
After adding continuously at a rate of 3 g / min and coating uniformly,
The product was cooled to a product temperature of 40 ° C. to obtain a fat-coated preparation of citric acid.

【0018】使用例1 実施例1で得られたL−アスコルビン酸の油脂被覆製剤
をゼラチンのハードカプセルに充填し、40℃にて1週
間保存したところ、対照とした油脂被覆しなかったL−
アスコルビン酸を充填したカプセルは褐色に変色したの
に対し、油脂被覆製剤を充填したものは全く変色しなか
った。 使用例2 実施例3で得られたL−アスコルビン酸の油脂被覆製剤
を、えび養殖用の飼料原料に配合し、加水、成形してモ
イストペレット製品にして保存したところ、対照とした
油脂被覆をしなかったL−アスコルビン酸は製造時およ
び保存中に短期間で分解したのに対し、油脂被覆製剤を
用いたものは、長期間残存していた。 使用例3 実施例5で得られたクエン酸の油脂被覆製剤を1%配合
したチューインガムを咀嚼したところ、油脂被覆しなか
ったクエン酸を用いた対照のチューインガムでは最初に
強い酸味があり、咀嚼中に短時間で酸味が弱まったのに
対し、油脂被覆製剤を配合したチューインガムでは、咀
嚼中の酸味の変化が少なく、長時間持続した。
Use Example 1 The oil- and fat-coated preparation of L-ascorbic acid obtained in Example 1 was filled in hard capsules of gelatin and stored at 40 ° C. for one week.
The capsules filled with ascorbic acid turned brown, while those filled with the oil-coated preparation did not change color at all. Use Example 2 The oil / fat coating formulation of L-ascorbic acid obtained in Example 3 was blended with a feed material for shrimp cultivation, added with water, molded and stored as a moist pellet product. L-ascorbic acid, which was not used, decomposed in a short period of time during production and storage, whereas that using an oil-coated preparation remained for a long period of time. Use Example 3 When chewing gum containing 1% of the oil-coated preparation of citric acid obtained in Example 5 was chewed, the control chewing gum using citric acid not coated with oil had a strong acidity at first, and during chewing. While the acidity weakened in a short time, the chewing gum containing the oil / fat coating preparation showed little change in the acidity during mastication and lasted for a long time.

【0019】[0019]

【発明の効果】以上記載したごとく、本発明によれば、
温度調節の可能な撹拌混合機装置のみで有機酸のよう
な、親水性の芯物質を、多量の被覆物質で多層被覆する
ことができ、しかも、水に浸漬しても芯物質の溶出が少
なく、芯物質の安定性の改良、風味の低減防止等が効果
的に期待できる。
As described above, according to the present invention,
A hydrophilic core substance, such as an organic acid, can be multi-layer coated with a large amount of a coating substance using only a stirring / mixing device capable of adjusting the temperature, and the elution of the core substance is small even when immersed in water. In addition, improvement of the stability of the core material, prevention of reduction in flavor, and the like can be expected effectively.

Claims (7)

【特許請求の範囲】[Claims] 【請求項1】 親水性の芯物質の周囲を複数の層の疎水
性熱溶融性の被覆物質で被覆した製剤の製造に際し、芯
物質を、被覆物質の固化温度以下の温度で混合しなが
ら、加熱溶融した被覆物質を連続的または分割して添加
しつつ、固化させ、芯物質の周囲に複数の被覆物質層を
形成させることを特徴とする被覆製剤の製造法。
In producing a preparation in which a hydrophilic core material is coated with a plurality of layers of a hydrophobic heat-meltable coating material, the core material is mixed at a temperature equal to or lower than the solidification temperature of the coating material. A method for producing a coated preparation, characterized by solidifying while continuously or separately adding a coating material that has been heated and melted to form a plurality of coating material layers around a core material.
【請求項2】 芯物質が、有機酸、有機酸塩類、非有機
酸系ビタミン類および糖類からなる群から選ばれる有機
物質である請求項1記載の製造法。
2. The method according to claim 1, wherein the core substance is an organic substance selected from the group consisting of organic acids, organic acid salts, non-organic acid vitamins and saccharides.
【請求項3】 芯物質がL−アスコルビン酸である請求
項2記載の被覆製剤の製造法。
3. The method according to claim 2, wherein the core substance is L-ascorbic acid.
【請求項4】 被覆物質が、油脂、脂肪酸、脂肪酸エス
テル類およびワックス類からなる群から選ばれる請求項
1記載の製造法。
4. The method according to claim 1, wherein the coating substance is selected from the group consisting of fats and oils, fatty acids, fatty acid esters and waxes.
【請求項5】 同じ被覆物質の層を複数形成させる請求
項1記載の製造法。
5. The method according to claim 1, wherein a plurality of layers of the same coating substance are formed.
【請求項6】 異なる被覆物質の層を形成させる請求項
1記載の製造法。
6. The method according to claim 1, wherein layers of different coating materials are formed.
【請求項7】 温度調整が可能な撹拌混合装置を用いて
被覆を行う請求項1記載の製造法。
7. The method according to claim 1, wherein the coating is performed using a stirring and mixing device capable of adjusting the temperature.
JP9013702A 1997-01-28 1997-01-28 Production of covered preparation Pending JPH10203965A (en)

Priority Applications (1)

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Publication Number Publication Date
JPH10203965A true JPH10203965A (en) 1998-08-04

Family

ID=11840549

Family Applications (1)

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Country Link
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Cited By (7)

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Publication number Priority date Publication date Assignee Title
US6485742B1 (en) 1999-04-05 2002-11-26 Basf Aktiengesellschaft Process for producing coated preparation and its use
JP2005537854A (en) * 2002-09-06 2005-12-15 アボット・ラボラトリーズ Medical device comprising a hydration inhibitor
JP2012521757A (en) * 2009-03-26 2012-09-20 アドバンスド バイオニュートリション コーポレーション Microencapsulation of biologically active substance and method for producing the same
JP2013128491A (en) * 2004-09-27 2013-07-04 Novozyme As Enzyme granule
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JP2021141849A (en) * 2020-03-12 2021-09-24 湯本製飴株式会社 Method for producing vitamin c, and vitamin c
CN114009474A (en) * 2021-10-19 2022-02-08 明富(上海)健康科技有限公司 Production equipment for embedding organic acid preservative by edible hydrogenated oil for baking, production process thereof and product

Cited By (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6485742B1 (en) 1999-04-05 2002-11-26 Basf Aktiengesellschaft Process for producing coated preparation and its use
JP2005537854A (en) * 2002-09-06 2005-12-15 アボット・ラボラトリーズ Medical device comprising a hydration inhibitor
JP2013128491A (en) * 2004-09-27 2013-07-04 Novozyme As Enzyme granule
JP2012521757A (en) * 2009-03-26 2012-09-20 アドバンスド バイオニュートリション コーポレーション Microencapsulation of biologically active substance and method for producing the same
US9445613B2 (en) 2009-03-26 2016-09-20 Advanced Bionutrition Corporation Microencapsulation of bioactive substances and methods of making the same
FR3077706A1 (en) * 2018-02-15 2019-08-16 Mixscience Composition against stress
WO2019158736A1 (en) * 2018-02-15 2019-08-22 Mixscience Anti-stress composition
JP2021141849A (en) * 2020-03-12 2021-09-24 湯本製飴株式会社 Method for producing vitamin c, and vitamin c
CN114009474A (en) * 2021-10-19 2022-02-08 明富(上海)健康科技有限公司 Production equipment for embedding organic acid preservative by edible hydrogenated oil for baking, production process thereof and product

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