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JPS62258327A - Production of coated powdery agent and coated granular agent - Google Patents

Production of coated powdery agent and coated granular agent

Info

Publication number
JPS62258327A
JPS62258327A JP10163386A JP10163386A JPS62258327A JP S62258327 A JPS62258327 A JP S62258327A JP 10163386 A JP10163386 A JP 10163386A JP 10163386 A JP10163386 A JP 10163386A JP S62258327 A JPS62258327 A JP S62258327A
Authority
JP
Japan
Prior art keywords
coating
coated
agent
water
coating composition
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.)
Granted
Application number
JP10163386A
Other languages
Japanese (ja)
Other versions
JPH0761962B2 (en
Inventor
Tetsunori Kitani
木谷 哲規
Isamu Takakura
高倉 勇
Kazuko Takaoka
高岡 和子
Setsuko Nishimura
節子 西村
Akira Takamichi
高道 章
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.)
Toyama Chemical Co Ltd
Original Assignee
Toyama Chemical 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 Toyama Chemical Co Ltd filed Critical Toyama Chemical Co Ltd
Priority to JP61101633A priority Critical patent/JPH0761962B2/en
Publication of JPS62258327A publication Critical patent/JPS62258327A/en
Publication of JPH0761962B2 publication Critical patent/JPH0761962B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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  • Medicinal Preparation (AREA)
  • Glanulating (AREA)

Abstract

PURPOSE:To produce a solid preparation having excellent moistureproofing property, free from pinhole and resistant to agglomeration, by using a coating composition produced by compounding a hardened oil and a water-soluble coating base at a specific ratio. CONSTITUTION:A coated powdery agent or coated granular agent is produced by coating powder, etc., with a coating composition composed of a hardened oil (e.g. paraffin wax, spermaceti, etc.) and a water-soluble coating base (e.g. methylcellulose) at a weight ratio of (4-9):1. The coating composition is used usually as a solution or dispersion in a proper solvent (e.g. methylene chloride) optionally in combination with various ajuvant (e.g. food dye, flavor, etc.). The coated powdery agent and coated granular agent produced by the above process is free from pinhole, resistant to agglomeration, capable of effectively preventing the compositional variation with small amount of coating material and releases the active component at a high rate.

Description

【発明の詳細な説明】 [産業上の利用分野] 本発明は、硬化油および水溶性コーティング基剤が4:
1〜9:1(重量比)からなるコーティング組成物を用
いて、コーティングすることを特徴とする被覆散剤およ
び被覆顆粒剤の製造方法に関する。本発明の目的は、粒
子径の小さい固形剤の配合性を向上させ、また、味を改
良した被覆散剤および被覆顆粒剤を提供することにある
DETAILED DESCRIPTION OF THE INVENTION [Industrial Application Field] The present invention provides a method in which the hydrogenated oil and the water-soluble coating base are 4:
The present invention relates to a method for producing coated powders and coated granules, which comprises coating using a coating composition having a ratio of 1 to 9:1 (weight ratio). An object of the present invention is to provide coated powders and coated granules with improved blendability of solid preparations having small particle diameters and improved taste.

[従来の技術] 従来、2種類以上の粒子径の小さい医薬品固形製剤の配
合投与において、それらの種類の異なる医薬成分同士の
相互作用により、色調に変化を生じたり変性や分解など
で効力が低下するなど好ましくないことがあった。その
ため、それらの相互作用を防止し、安定かつ有効な製剤
とするために、また、各種の固形製剤についてその不快
な味を隠蔽し、服用し易くするために、それらを各種の
被膜形成性のおる物質でコーティングすることが行われ
ている。
[Prior art] Conventionally, when administering a combination of two or more types of solid pharmaceutical preparations with small particle sizes, interactions between the different types of pharmaceutical ingredients can cause changes in color tone, denaturation, decomposition, etc., resulting in decreased efficacy. There were some undesirable things that happened. Therefore, in order to prevent these interactions and make the preparations stable and effective, as well as to hide the unpleasant taste of various solid preparations and make them easier to take, various film-forming agents have been added to them. coating with a substance that

コーティング基剤として使用される被膜形成性のおる物
質としては、水溶性のセルロース誘導体が一般に使用さ
れることは公知でおる。
It is well known that water-soluble cellulose derivatives are generally used as film-forming substances used as coating bases.

また、硬化油も医薬品の被覆材料として用いられている
(たとえば、特開昭−9713号など)。
Furthermore, hydrogenated oils are also used as coating materials for pharmaceuticals (for example, Japanese Patent Application Laid-Open No. 9713/1993).

[発明が解決しようとする問題点] 粒子径の小ざい固形剤、たとえば、散剤および顆粒剤は
取扱いの容易さにより、仙薬剤と配合されて投薬される
が、配合時に異なる医薬品同士の相互作用のために変性
や分解で効力が低下する場合、前記したコーティングが
必要である。
[Problems to be solved by the invention] Solid preparations with small particle diameters, such as powders and granules, are easily handled and are administered by combining them with a herbal medicine. If the efficacy is reduced due to denaturation or decomposition, the above-mentioned coating is necessary.

しかしながら、水溶性セルロース誘導体を用いて粒子径
の小ざい固形剤、たとえば、散剤、顆粒剤をコーティン
グする場合、これらは単位重追当たりの表面積が大きい
ため、錠剤にコーティングする場合に比べ、コーテイン
グ量を多くする必要がある。
However, when coating solid drugs with small particle sizes, such as powders and granules, with water-soluble cellulose derivatives, the amount of coating is larger than when coating tablets because these have a large surface area per unit weight. It is necessary to increase the number of

また、これらのコーティングには、通常、コーティング
パン、流動層コーティング装置、遠心流動コーティング
装置などが用いられるが、その場合、粒子同士が結合し
大きな粒子に成長する、いわゆる団粒現象を起こし易い
Furthermore, coating pans, fluidized bed coating devices, centrifugal fluidized coating devices, and the like are usually used for these coatings, but in that case, particles tend to bond with each other and grow into large particles, which is the so-called agglomeration phenomenon.

さらに、この団粒現象はコーテイング量が多くなるほど
、また粒子が小さくなるほど起こりやすい。
Furthermore, this agglomeration phenomenon is more likely to occur as the amount of coating increases and as the particles become smaller.

この団粒現象を抑制する方法として、コーティング組成
物中に、たとえば、タルク、糖類および粉末の錠剤用崩
壊剤などを加え、分散させた液剤をスプレーすることが
試みられているが、スプレーガンのつまりなどの支障が
多く、また必ずしも充分な効果は認められないのが実情
である。
As a method to suppress this agglomeration phenomenon, attempts have been made to add, for example, talc, sugar, and a powdered tablet disintegrant to the coating composition and spray a dispersed liquid. The reality is that there are many problems such as this, and that sufficient effects are not always recognized.

コーティング基剤として硬化油を単独に用いて、粒子径
の小さい固形剤、たとえば、散剤および顆粒剤をコーテ
ィングすると、ピンホールを生じ、安全性において問題
があり、ざらに、溶出時間が遅延する傾向にあるので好
ましくない。
When hardened oil is used alone as a coating base to coat solid agents with small particle sizes, such as powders and granules, pinholes occur, which poses safety problems, and tends to result in roughness and delayed dissolution time. It is not desirable because it is in

[問題点を解決する手段] 本発明者らは上記問題点を解決するために、粒子径の小
さい固形剤、たとえば、散剤および顆粒剤のコーティン
グにおいて出来るだけ少ないコーテイング量でしかもコ
ーティング操作中に造粒または団粒を起こさず、十分な
コーティング効果、たとえば、配合禁忌品目との配合を
可能にしたり、味の改善、防湿性の向上などをもたらす
コーティング方法について鋭意研究を行った。
[Means for Solving the Problems] In order to solve the above problems, the present inventors have developed a method for coating solid agents with small particle sizes, such as powders and granules, with as little coating amount as possible and during the coating operation. We have conducted intensive research on coating methods that do not cause grains or aggregates and provide sufficient coating effects, such as enabling combination with prohibited items, improving taste, and improving moisture resistance.

その結果、硬化油および水溶性コーティング基剤が4=
1〜9:1(重ffi比)からなるコーティング組成物
を用いて、粒子径の小さい固形剤、たとえば、散剤およ
び顆粒剤、特に、細粒剤をコーティングすると、防湿性
に優れ、ピンホールがなく、団粒化なども起さない優れ
た固形剤に製剤化できることを見出し、本発明を完成し
た。
As a result, the hydrogenated oil and water-soluble coating base are 4=
When solid agents with small particle sizes, such as powders and granules, especially fine granules, are coated with a coating composition consisting of a ratio of 1 to 9:1 (heavy ffi ratio), they have excellent moisture resistance and are free from pinholes. The present invention was completed based on the discovery that it is possible to formulate an excellent solid preparation that does not cause any agglomeration or agglomeration.

以下、本発明の詳細な説明する。The present invention will be explained in detail below.

本発明に使用される硬化油としては、製剤上許容される
ものであれば、植物性、動物性のいずれでもよく、たと
えば、パラフィンロウ、カルプウバロウ、鯨ロウ、蜜ロ
ウ、カスターワックス(Caster Wax)、硬化
牛油、硬化植物油1.たとえば、硬化ヒマシ油、硬化ナ
タネ油、硬化ラッカセイ油などが挙げられる。
The hardened oil used in the present invention may be either vegetable or animal as long as it is pharmaceutically acceptable, such as paraffin wax, carp wax, spermaceti, beeswax, and caster wax. , hydrogenated beef oil, hydrogenated vegetable oil 1. Examples include hydrogenated castor oil, hydrogenated rapeseed oil, and hydrogenated peanut oil.

また、水溶性コーティング基剤としては、たとえば、メ
チルセルロース、ヒドロキシエチルセルロース、ヒドロ
キシプロピルセルロース、ヒドロキシエチルメチルセル
ロース、ヒドロキシプロピルメチルセルロース、ヒドロ
キシブチルセルロースなどが挙げられる。
Examples of water-soluble coating bases include methylcellulose, hydroxyethylcellulose, hydroxypropylcellulose, hydroxyethylmethylcellulose, hydroxypropylmethylcellulose, and hydroxybutylcellulose.

硬化油と水溶性コーティング基剤の組み合わせで好まし
いものとしては、硬化ナタネ油とヒドロキシプロピルメ
チルセルロースとの組み合わせが挙げられる。
A preferred combination of hydrogenated oil and water-soluble coating base is a combination of hydrogenated rapeseed oil and hydroxypropyl methylcellulose.

コーティング組成物における硬化油と水溶性コーティン
グ基剤の混合比は4:1〜9:1(重重比)である。
The mixing ratio of hardened oil and water-soluble coating base in the coating composition is 4:1 to 9:1 (weight ratio).

また、コーテイング量は対象未コーティング剤のmff
1に対し、1〜20重量%、好ましくは3〜10重量%
である。
In addition, the coating amount is mff of the target uncoated agent.
1 to 20% by weight, preferably 3 to 10% by weight based on 1
It is.

本発明において使用される硬化油と水溶性コーティング
基剤からなるコーティング組成物は通常適当な溶媒中に
溶解、分散(コーテイング液)させて使用され、この場
合、溶媒としては、塩化メチレン、クロロホルムなどの
ハロゲン化炭化水素類;メタノール、エタノールなどの
アルコール類/ハロゲン化炭化水素類:アセトン/ハロ
ゲン化炭化水素類;水/アルコール類/ハロゲン化炭化
水素類などの単一溶媒あるいは混合溶媒が挙げられる。
The coating composition composed of a hardened oil and a water-soluble coating base used in the present invention is usually dissolved and dispersed in a suitable solvent (coating liquid). In this case, the solvent may be methylene chloride, chloroform, etc. halogenated hydrocarbons; alcohols such as methanol and ethanol; halogenated hydrocarbons; acetone/halogenated hydrocarbons; single solvents or mixed solvents such as water/alcohols/halogenated hydrocarbons. .

また、必要に応じて適当な湿度で溶解させるのが好まし
い。
Moreover, it is preferable to dissolve it at an appropriate humidity as necessary.

コーテイング液中における硬化油と水溶性コーティング
基剤の濃度は、全固形成分が、1〜10重量%、好まし
くは2〜5@量%でおる。
The concentration of the hardened oil and the water-soluble coating base in the coating liquid is such that the total solid component is 1 to 10% by weight, preferably 2 to 5% by weight.

このようにして得られるコーテイング液には各種の助剤
を含有させてもよく、たとえば、食用色素、食用レーキ
、酸化チタンなどの着色剤、グリセリン脂肪酸エステル
類、ポリエチレングリコール類、プロピレングリコール
類などの可塑剤、シリコーンオイル、界面活性剤、香料
などが挙げられる。
The coating solution obtained in this way may contain various auxiliary agents, such as coloring agents such as food dyes, food lakes, and titanium oxide, glycerin fatty acid esters, polyethylene glycols, and propylene glycols. Examples include plasticizers, silicone oils, surfactants, and fragrances.

本発明方法には通常遠心流動コーティング装置が使用さ
れるが、そのほか、流動層コーティング装置も使用する
ことができる。
Although a centrifugal fluid coating device is usually used in the method of the present invention, a fluidized bed coating device can also be used.

なあ、スプレー用のガンは、一般に使用されているもの
でよい。
By the way, any commonly used spray gun will suffice.

[発明の効果] (1)配合変化試験 実施例および参考例の製剤と酸化マグネシウムを3:2
(重量比)に配合し、40’C−相対湿度75%の条件
下で放置し、配合品中のビス(2−トリメチルアンモニ
オエチル−α−アセトキシプロピオネート)−ナフタレ
ン−1,5−ジスルホネート(一般名:ナパジシル酸ア
クラドニウム、以下、ナパジシル酸アクラドニウムと称
する。)の定m値に対する放置後の配合品中のナパジシ
ル酸アクラドニウムの定量値を相対百分率として算出し
残存率とした。その結果を表−1に示す。
[Effects of the invention] (1) Formulations of blend change test examples and reference examples and magnesium oxide at a ratio of 3:2
(weight ratio) and left under the conditions of 40'C and 75% relative humidity. The quantitative value of acladonium napadisylate in the compounded product after standing with respect to the constant m value of disulfonate (generic name: acradonium napadisylate, hereinafter referred to as acradonium napadisylate) was calculated as a relative percentage and was defined as the residual rate. The results are shown in Table-1.

なお、ナパジシル酸アクラドニウムの定量はブロムクレ
ゾールグリーン比色法、すなわち、ナパジシル酸アクラ
ドニウムとブロムクレゾールグリーンを結合させ、これ
をクロロホルムで抽出し、次いで水酸化ナトリウム液を
加え、振り混ぜた後水層に逆抽出されたブロムクレゾー
ルグリーンを吸光光度法で定量することにより行った。
The determination of acradonium napadisylate was carried out using the bromcresol green colorimetric method, that is, acladonium napadisylate and bromcresol green were combined, extracted with chloroform, and then a sodium hydroxide solution was added, shaken, and then added to the aqueous layer. This was done by quantifying the back-extracted bromcresol green by spectrophotometry.

(以下余白〉 (2)溶出試験 日本薬局方(第10改正)溶出試験法(パドル法、11
00pp、崩壊試験法で用いられる第1液800dを使
用)に従って吸光光度法によりナパジシル酸アクラドニ
ウムの溶出量を測定し、)8出率が75%に達するまで
の時間(T75)を算出した。
(Left below) (2) Dissolution test Japanese Pharmacopoeia (10th revision) Dissolution test method (paddle method, 11
The elution amount of acladonium napadisylate was measured by spectrophotometry according to the method (using the first liquid 800d used in the disintegration test method), and the time (T75) until the elution rate reached 75% was calculated.

その結果を表−2に示す。The results are shown in Table-2.

表−2 以上の結果より本発明のコーティング方法により製造さ
れる被覆散剤および被覆顆粒剤はピンホールを生ぜず(
図−1および図−2参照)、また団粒化ぜずに、少ない
コーテイング量で配合変化を効果的に防止する事かでき
、また、こうして1りられた被覆剤は良好な溶出を示す
事が理解できる。
Table 2 From the above results, the coated powders and coated granules produced by the coating method of the present invention do not produce pinholes (
(Refer to Figures 1 and 2), it is possible to effectively prevent changes in the formulation with a small amount of coating without causing agglomeration, and the coating agent thus removed exhibits good dissolution. I can understand.

ざらに、硬化油単独でコーティングされた被覆散剤およ
び被覆顆粒剤で感じられる舌ざわりの悪さも解消され、
しかも、内部の薬剤の味は隠蔽されている。
In addition, the unpleasant texture felt by coated powders and coated granules coated with hydrogenated oil alone is also eliminated.
Moreover, the taste of the medicine inside is hidden.

[実施例] 次に、本発明を実施例および参考例を挙げて説明するが
本発明はこれらに限定されるものではない。
[Examples] Next, the present invention will be described with reference to Examples and Reference Examples, but the present invention is not limited thereto.

なお、実施例および参考例で、グラニユー糖、遠心流動
コーテイング機、5%ヒドロキシプロピルメチルセルロ
ース、乳糖、硬化ナタネ油、ヒドロキシプロピルメチル
セルロース、マンニット、コンスターチ、酸化エチレン
・酸化プロピレン共重物はそれぞれ次のものを使用した
In addition, in Examples and Reference Examples, granulated sugar, centrifugal fluid coating machine, 5% hydroxypropyl methylcellulose, lactose, hydrogenated rapeseed oil, hydroxypropyl methylcellulose, mannitol, cornstarch, and ethylene oxide/propylene oxide copolymer are as follows. I used something.

0グラニユー糖[60−80メツシュ:塩水港製糖(株
)製] 0遠心流動コ一テイング機[CF−360:フロイント
産業(株)製] 05%ヒドロキシプロピルメチルセルロース[HPC−
L :日本曹達(株)製] 0乳糖[MiCrOtO3e :メグレ(株)製]0硬
化ナタネ油[ラブリラックス102;フロイント産業(
株)製] 0ヒドロキシプロピルメチルセルロース[TC−5RW
;信越化学(株)製] Oマンニット[乗和化成(株)製] Oコンスターチ[北陸砂糖(株)製] 0r!i化エチレン・酸化プロピレン共重物[PEP−
101:フロイント産業(株)製−]実施例1 (1)グラニユー糖1400gを遠心流動コーテイング
機に仕込み、5%ヒドロキシプロピルメチルセルロース
含水エタノール溶液[水:エタノール=1 :3.25
 (重量比)] 1040gを噴霧しながらナバジシル
葭アクラドニウム302.1および乳糖625.6gの
混合物を粉体コーティングする。引き続き、連続操作で
乳糖420gを粉体コーティングする。生成した粒子を
40℃で一夜乾燥すれば、コーティング用の細粒275
29を得る。
0 Granulated sugar [60-80 mesh: manufactured by Shiomiko Sugar Co., Ltd.] 0 Centrifugal fluid coating machine [CF-360: manufactured by Freund Sangyo Co., Ltd.] 05% hydroxypropyl methylcellulose [HPC-
L: manufactured by Nippon Soda Co., Ltd.] 0 lactose [MiCrOtO3e: manufactured by Megre Co., Ltd.] 0 hydrogenated rapeseed oil [Love Relax 102; Freund Sangyo (
Co., Ltd.] 0 hydroxypropyl methylcellulose [TC-5RW
; Manufactured by Shin-Etsu Chemical Co., Ltd.] O Mannit [manufactured by Noriwa Kasei Co., Ltd.] O Cornstarch [manufactured by Hokuriku Sugar Co., Ltd.] 0r! I-ized ethylene/propylene oxide copolymer [PEP-
101: Manufactured by Freund Sangyo Co., Ltd.] Example 1 (1) 1400 g of granulated sugar was charged into a centrifugal flow coating machine, and a 5% hydroxypropyl methyl cellulose water-containing ethanol solution [water:ethanol = 1:3.25] was prepared.
(Weight ratio)] Powder coat a mixture of Navadicil Yoshi Acladonium 302.1 and lactose 625.6 g while spraying 1040 g. Subsequently, 420 g of lactose is powder coated in a continuous operation. If the generated particles are dried overnight at 40°C, fine particles 275 for coating can be obtained.
Get 29.

(2) (1)で得られたコーティング用細粒5009
を遠心流動コーテイング機に仕込み、硬化ナタネ油48
.6gおよびヒドロキシプロピルメチルセルロース5.
4gを塩化メチレン1674cJおよびエタノール43
2gの混液に溶解させた液(以下、コーテイング液Aと
称する。)を噴霧し、コーティングする。生成した粒子
を40’Cで一夜乾燥すれば、細粒剤545gを得る。
(2) Coating fine particles 5009 obtained in (1)
into a centrifugal fluid coating machine, hardened rapeseed oil 48
.. 6g and hydroxypropyl methylcellulose5.
4 g of methylene chloride 1674 cJ and ethanol 43
A solution (hereinafter referred to as coating solution A) dissolved in 2 g of the mixed solution is sprayed to coat. Drying the resulting particles at 40'C overnight yields 545 g of fine granules.

実施例2 実施例1(1)のコーティング用細粒500gに対して
、硬化ナタネ油30.19およびヒドロキシプロピルメ
チルセルロース7.59を塩化メチレン1164.89
およびエタノール300.69の混液に溶解させた液(
以下、コーテイング液Bと称する。)を噴霧し、コーテ
ィングする。生成した粒子を40°Cで一夜乾燥すれば
、細粒剤5333を得る。
Example 2 30.19 g of hardened rapeseed oil and 7.59 hydroxypropyl methylcellulose were added to 1164.89 g of methylene chloride for 500 g of coating fine particles of Example 1 (1).
and a solution dissolved in a mixture of ethanol 300.69 (
Hereinafter, it will be referred to as coating liquid B. ) and coat. Fine granules 5333 are obtained by drying the produced particles at 40° C. overnight.

実施例3 (1)グラニュー1!11400yを遠心流動コーテイ
ング機に仕込み、5%ヒドロキシプロピルメチルセルロ
ース含水エタノール溶液[水:エタノール=1ニア、5
(重量比)1823yを噴霧しながらナパジシル酸アク
ラドニウム280gとマンニット4203の混合物を粉
体コーティングする。
Example 3 (1) Granules 1!11400y were charged into a centrifugal flow coating machine, and a 5% hydroxypropyl methyl cellulose water-containing ethanol solution [water: ethanol = 1 nia, 5
A mixture of 280 g of acladonium napadisylate and Mannitol 4203 is powder coated while spraying 1823y (weight ratio).

引き続き、連続操作でマンニット2803およびコーン
スターチ4203の混合物を粉体コーティングする。生
成した粒子を40°Cで一夜乾燥すれば、コーティング
用の細粒2781を得る。
Subsequently, a mixture of Mannitol 2803 and Cornstarch 4203 is powder coated in a continuous operation. Drying the resulting particles at 40° C. overnight provides fine particles 2781 for coating.

(2) (1)で1qられたコーティング用細粒600
9に対して、コーテイング液A1247cJを噴霧し、
コーティングする。生成した粒子を40’Cで一夜乾燥
すれば、細粒剤6209を得る。
(2) Fine particles for coating 600 obtained by 1q in (1)
9, spray coating liquid A1247cJ,
Coat. Fine granules 6209 are obtained by drying the produced particles at 40'C overnight.

実施例4 実施例3(1)で得られたコーティング用細粒406g
に対して、コーテイング液B8869を噴霧し、コーテ
ィングする。生成した粒子を40°Cで一夜乾燥すれば
、細粒剤4229を得る。
Example 4 406 g of fine particles for coating obtained in Example 3 (1)
Coating liquid B8869 is sprayed onto the sample to coat it. Fine granules 4229 are obtained by drying the resulting particles at 40° C. overnight.

参考例1 実施例3(1)で得られたコーティング用細粒5009
に対して、硬化ナタネ油34.1を塩化メチレン113
1.9gおよびエタノール205.89の混液に溶解さ
せた液を噴霧し、コーティングする。生成した粒子を4
0’Cで一夜乾燥すれば、細粒剤524gを得る。
Reference Example 1 Coating fine particles 5009 obtained in Example 3 (1)
For hydrogenated rapeseed oil 34.1 to methylene chloride 113
Spray and coat with a mixture of 1.9 g and 205.89 g of ethanol. The generated particles are 4
Drying overnight at 0'C yields 524 g of fine granules.

参考例2 実施例3(1)で得られたコーティング用細粒5003
に対して、ヒドロキシプロピルメチルセルロース19.
8gおよび酸化エチレン・酸化プロピレン共重合物2.
O12を塩化メヂレン612.1、エタノール158.
1および水10.3!?の混液に溶解させた液を噴霧し
、コーティングする。生成した粒子を40°Cで一夜乾
燥すれば、細粒剤509gを得る。
Reference Example 2 Fine particles for coating 5003 obtained in Example 3 (1)
against hydroxypropyl methylcellulose 19.
8g and ethylene oxide/propylene oxide copolymer2.
O12 was mixed with 612.1% of medilene chloride and 158.1% of ethanol.
1 and water 10.3! ? Spray the solution dissolved in the mixture to coat. Drying the produced particles at 40°C overnight yields 509 g of fine granules.

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

図−1および図−2の写真(走査型電子顕微鏡、倍率ニ
ア0倍)はそれぞれ参考例1、実施例1の細粒剤を示す
The photographs in Figures 1 and 2 (scanning electron microscope, near 0x magnification) show the fine granules of Reference Example 1 and Example 1, respectively.

Claims (2)

【特許請求の範囲】[Claims] (1)硬化油および水溶性コーティング基剤が4:1〜
9:1(重量比)からなるコーティング組成物を用いて
、コーティングすることを特徴とする被覆散剤および被
覆顆粒剤の製造方法。
(1) Hydrogenated oil and water-soluble coating base of 4:1 or more
A method for producing coated powders and coated granules, which comprises coating using a coating composition having a weight ratio of 9:1.
(2)被覆散剤が被覆細粒剤である特許請求の範囲第(
1)項記載の被覆散剤の製造方法。
(2) Claim No. 2, wherein the coated powder is a coated fine granule (
1) The method for producing the coated powder described in section 1).
JP61101633A 1986-05-01 1986-05-01 Method for producing coated fine granules Expired - Fee Related JPH0761962B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP61101633A JPH0761962B2 (en) 1986-05-01 1986-05-01 Method for producing coated fine granules

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP61101633A JPH0761962B2 (en) 1986-05-01 1986-05-01 Method for producing coated fine granules

Publications (2)

Publication Number Publication Date
JPS62258327A true JPS62258327A (en) 1987-11-10
JPH0761962B2 JPH0761962B2 (en) 1995-07-05

Family

ID=14305801

Family Applications (1)

Application Number Title Priority Date Filing Date
JP61101633A Expired - Fee Related JPH0761962B2 (en) 1986-05-01 1986-05-01 Method for producing coated fine granules

Country Status (1)

Country Link
JP (1) JPH0761962B2 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2012051831A (en) * 2010-08-31 2012-03-15 Fancl Corp Method for producing mixed granulate

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS55149211A (en) * 1979-05-10 1980-11-20 Takeda Chem Ind Ltd Production of gradually releasable preparation
JPS5721314A (en) * 1980-07-11 1982-02-04 Yamanouchi Pharmaceut Co Ltd Composition for pharmaceutical preparation free from bitter taste, and its preparation

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS55149211A (en) * 1979-05-10 1980-11-20 Takeda Chem Ind Ltd Production of gradually releasable preparation
JPS5721314A (en) * 1980-07-11 1982-02-04 Yamanouchi Pharmaceut Co Ltd Composition for pharmaceutical preparation free from bitter taste, and its preparation

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2012051831A (en) * 2010-08-31 2012-03-15 Fancl Corp Method for producing mixed granulate

Also Published As

Publication number Publication date
JPH0761962B2 (en) 1995-07-05

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