JPS62135419A - Granular composition of diclofenac salt and production thereof - Google Patents

Granular composition of diclofenac salt and production thereof

Info

Publication number
JPS62135419A
JPS62135419A JP27478585A JP27478585A JPS62135419A JP S62135419 A JPS62135419 A JP S62135419A JP 27478585 A JP27478585 A JP 27478585A JP 27478585 A JP27478585 A JP 27478585A JP S62135419 A JPS62135419 A JP S62135419A
Authority
JP
Japan
Prior art keywords
water
diclofenac
granules
diclofenac salt
coating
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
JP27478585A
Other languages
Japanese (ja)
Inventor
Teruo Mizukami
水上 輝夫
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.)
IKEDA MOHANDOU KK
Original Assignee
IKEDA MOHANDOU KK
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 IKEDA MOHANDOU KK filed Critical IKEDA MOHANDOU KK
Priority to JP27478585A priority Critical patent/JPS62135419A/en
Publication of JPS62135419A publication Critical patent/JPS62135419A/en
Pending legal-status Critical Current

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Classifications

    • AHUMAN NECESSITIES
    • A61MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61KPREPARATIONS FOR MEDICAL, DENTAL OR TOILETRY PURPOSES
    • A61K9/00Medicinal preparations characterised by special physical form
    • A61K9/14Particulate form, e.g. powders, Processes for size reducing of pure drugs or the resulting products, Pure drug nanoparticles
    • A61K9/16Agglomerates; Granulates; Microbeadlets ; Microspheres; Pellets; Solid products obtained by spray drying, spray freeze drying, spray congealing,(multiple) emulsion solvent evaporation or extraction
    • A61K9/167Agglomerates; Granulates; Microbeadlets ; Microspheres; Pellets; Solid products obtained by spray drying, spray freeze drying, spray congealing,(multiple) emulsion solvent evaporation or extraction with an outer layer or coating comprising drug; with chemically bound drugs or non-active substances on their surface
    • A61K9/1676Agglomerates; Granulates; Microbeadlets ; Microspheres; Pellets; Solid products obtained by spray drying, spray freeze drying, spray congealing,(multiple) emulsion solvent evaporation or extraction with an outer layer or coating comprising drug; with chemically bound drugs or non-active substances on their surface having a drug-free core with discrete complete coating layer containing drug

Landscapes

  • Engineering & Computer Science (AREA)
  • Bioinformatics & Cheminformatics (AREA)
  • Health & Medical Sciences (AREA)
  • Chemical & Material Sciences (AREA)
  • Medicinal Chemistry (AREA)
  • Pharmacology & Pharmacy (AREA)
  • Epidemiology (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Animal Behavior & Ethology (AREA)
  • General Health & Medical Sciences (AREA)
  • Public Health (AREA)
  • Veterinary Medicine (AREA)
  • Acyclic And Carbocyclic Compounds In Medicinal Compositions (AREA)

Abstract

PURPOSE:The titled composition, obtained by uniformly coating the surface of small granular cores with a diclofenac salt and a binder and having improved stability. CONSTITUTION:A granular composition of a diclofenac salt obtained by dissolving 1-30% diclofenac salt, e.g. diclofenac sodium, etc., and 0.1-5% binder, e.g. mixture of one or two or more or water-soluble high polymers, pH- dependent high polymers and water-insoluble high polymers, polyvinylpyrrolidone, ethyl cellulose or eudragit, etc., in water.organic solvent, e.g. water.ethanol, etc., and spray coating small granular cores with the resultant solution. Furthermore, coating with a sustained release film, enteric coating, etc., may be carried out to give a continuous multi-layered material. EFFECT:The solution is readily prepared and the subsequent production process can be continuously performed without requiring any lubricant, etc., and scattering of powder.

Description

【発明の詳細な説明】 〔産業上の利用分野〕 本発明は化学的性質及び物理的性質特に安定性に俊れた
、ジクロフェナク塩の粒状組成物及びその製造法に関す
るものである。
DETAILED DESCRIPTION OF THE INVENTION [Field of Industrial Application] The present invention relates to a granular composition of diclofenac salt having excellent chemical and physical properties, particularly stability, and a method for producing the same.

〔従来の技術ならびにそれらの問題点〕ジクロフェナク
塩〔化学名:2−(2,6−ジクロロアニリノ)フェニ
ル酢酸の塩〕は、消炎・鎮痛性を有する物質であること
が知られている。
[Prior Art and Their Problems] Diclofenac salt [chemical name: 2-(2,6-dichloroanilino)phenylacetic acid salt] is known to be a substance having anti-inflammatory and analgesic properties.

そのナトリウム塩は、内服製剤としては、例えば錠剤、
顆粒、細粒として製剤化され用いられている。
The sodium salt can be used in oral preparations such as tablets,
It is formulated and used as granules and fine granules.

ところで顆粒の製造方法としては、薬物と賦形剤、結合
剤、崩壊剤、滑沢剤等の混合粉末を、圧縮・粗砕する方
法、適当な溶媒を加えて練合し造粒する方法、小粒状核
に薬物と賦形剤との混合粉末を被覆する方法等が考えら
れる。
By the way, methods for producing granules include compressing and crushing a mixed powder of drugs, excipients, binders, disintegrants, lubricants, etc.; methods of kneading and granulating by adding an appropriate solvent; Possible methods include coating small granular cores with a mixed powder of a drug and an excipient.

また錠剤の製造方法としては、前記顆粒に滑沢剤等を加
え、圧縮成形して製造するか、薬物と賦形剤、結合剤、
崩壊剤、滑沢剤等の混合粉末を直接圧縮成形して製造す
る方法が考えられる。
In addition, the tablets can be manufactured by adding a lubricant etc. to the granules and compression molding, or by adding a lubricant etc. to the granules and manufacturing by compression molding, or by adding a drug, an excipient, a binder, etc.
A method of manufacturing by directly compression molding a mixed powder of a disintegrant, a lubricant, etc. can be considered.

しかして上記の製造方法において、薬物は−、役に粉末
状態で製剤化されるが、薬物を溶液に溶解させた状態で
製剤化する公知の方法としては、例えばニカルジピンと
pl+依存性添加剤及び/又は水溶性高分子を有機溶媒
に溶解し、小粒状核に被覆してニカルジピンの小粒状の
顆粒を製造する方法(特開昭58−116414号公報
)や、ニフェジピンと水溶性高分子及び/又は水不溶性
高分子及び/又はpH依存性添加剤を、有機溶媒に溶解
し細粒に被覆してニフェジピン製剤を製造する方法(特
開昭57=85316号公報、特開昭58−77811
号公報)等が知られている。
However, in the above manufacturing method, the drug is formulated in powder form, but known methods for preparing the drug in a solution form include, for example, nicardipine, a PL+ dependent additive, and A method of producing small granules of nicardipine by dissolving a water-soluble polymer in an organic solvent and coating the small granular cores (Japanese Patent Application Laid-open No. 116414/1982), Alternatively, a method for producing a nifedipine preparation by dissolving a water-insoluble polymer and/or a pH-dependent additive in an organic solvent and coating it on fine particles (JP-A-57-85316, JP-A-58-77811)
Publication No.) etc. are known.

しかして前述のような従来技術における顆粒の製造には
、各種欠点があった。例えば小粒状核に薬物と賦形剤の
混合粉末を被覆する方法においては、篩過・混合・乾燥
等の粉末の調製が煩雑で、そのため時間がかかった。更
に小粒状に被覆する条件により、製造中に顆粒どうしが
付着し団粒となったり、被覆粉末の損失による薬剤の含
量低下等の欠点があった。
However, the production of granules in the prior art as described above has various drawbacks. For example, in the method of coating small granular cores with a mixed powder of a drug and an excipient, preparation of the powder such as sieving, mixing, and drying is complicated and therefore time consuming. Furthermore, due to the conditions for coating small particles, there were disadvantages such as granules adhering to each other and forming aggregates during production, and loss of coated powder resulting in a decrease in drug content.

また、賦形剤を添加すると顆粒の形状が大きくなり、そ
のため製造された顆粒をカプセル剤にする場合、カプセ
ルを大きくしなければならず、しかも薬物の安定性を考
危すると必ずしも好ましい方法ということができないも
のであった。
In addition, adding excipients increases the size of the granules, so if the manufactured granules are to be made into capsules, the capsules must be made larger, and this method is not necessarily preferable considering the stability of the drug. It was impossible.

更にジクロフェナク塩の場合、比較的水に溶けやすいた
め、水に難溶性の賦形剤との間に溶解度差が生じ、顆粒
表面に凹凸の出来ることがある。
Furthermore, in the case of diclofenac salt, since it is relatively easily soluble in water, a solubility difference may occur between the diclofenac salt and an excipient that is sparingly soluble in water, resulting in unevenness on the surface of the granules.

このことは顆粒表面にさらに薬物透過性皮膜等を被覆し
徐放性顆粒を製造することを考えると、通常、顆粒表面
は平滑で、かつ薬物含量のバラツキが小さいことが必要
であることから考えて、賦形剤の使用は余り好ましいも
のではなかった。
This is because when considering that sustained release granules are manufactured by coating the granule surface with a drug-permeable film, etc., the granule surface usually needs to be smooth and the variation in drug content should be small. Therefore, the use of excipients was not very favorable.

また、賦形剤を使用せず、薬物と水溶性高分子を有機溶
媒に溶解し、小粒状核に被覆する場合、従来の方法では
多くのハロゲン系有機溶媒(ジクロルメタン等)を必要
とし、排気による環境汚染、製造時の安全性及び製剤中
へのコーティング溶媒の残留の点で問題があり、かつ作
業時間も比較的かかり、実用的方法ではないという難点
があった7本発明は以上の問題点を改善または解決しよ
うとするものである。すなわち製法が簡単であり、粒状
顆粒表面を平滑にし、薬剤の各顆粒における含量のバラ
ツキが少なく、かつ安定な粒状顆粒を4ることを目的と
する。
In addition, when dissolving drugs and water-soluble polymers in organic solvents and coating them on small granular nuclei without using excipients, conventional methods require a large amount of halogen-based organic solvents (dichloromethane, etc.) and exhaust gas. The present invention has problems in terms of environmental pollution, safety during manufacturing, and residual coating solvent in the formulation, and is relatively time-consuming and not a practical method.7 The present invention solves the above problems. This is an attempt to improve or solve a problem. That is, the purpose is to provide stable granules that are easy to manufacture, have smooth granule surfaces, have little variation in drug content in each granule, and are stable.

〔問題点を解決するための手段〕[Means for solving problems]

本発明者らは、上記目的(粒状顆粒の安定性、同顆粒の
表面の平滑性並びに作業性の改悠)を達成するため、賦
形剤を用いることなく、しかも作業上溶媒の残留性等の
改善を併せ有する粒状顆粒及びその製造法について種々
研究を行なった。その結果、ジクロフェナク塩がエタノ
ール等の有機溶媒に溶けやすく、水にやや溶けにくいが
、水〜有機溶媒(特にエタノール)の混合溶媒において
、溶解度が増大するという特性を見出し、この溶媒に結
合剤とジクロフェナク塩とを溶解し、小粒状核に被覆す
ることによって、極めて良好な顆粒を製造し得る本発明
に到達した。
In order to achieve the above objectives (stability of granules, smoothness of the surface of the granules, and improvement in workability), the present inventors have achieved the goal of improving the stability of granules, improving the surface smoothness of the granules, and improving workability without using any excipients, and without using any excipients. Various studies have been conducted on granules that have improved properties and methods for producing them. As a result, we found that diclofenac salt is easily soluble in organic solvents such as ethanol, and slightly less soluble in water, but its solubility increases in a mixed solvent of water and organic solvents (especially ethanol). The present invention has been achieved in which extremely good granules can be produced by dissolving diclofenac salt and coating it on small granular cores.

この顆粒の製造法によれば、溶液の調製は容易であり、
被覆作業中も顆粒の団粒は見られず、滑沢剤等が全く不
要であり、粉の飛散もなく、引き続いての製剤工程が連
続して実施可能であるという特長を有する。また得られ
たジクロフェナク塩顆粒が、安定性に優れ、使用するジ
クロフェナク塩の結晶形にかかわらず表面のジクロフェ
ナク塩の結晶形が微細であり、顆粒表面の凹凸がなく平
滑であり、つぎの製造工程に対しても取り扱いがよく、
しかも各粒状顆粒に含有する薬剤の量にバラツキが少な
いという特長を有する。
According to this granule production method, the solution is easy to prepare;
No granule agglomerations are observed during the coating process, no lubricants are required, there is no scattering of powder, and the subsequent formulation process can be carried out continuously. In addition, the obtained diclofenac salt granules have excellent stability, and regardless of the crystal form of the diclofenac salt used, the crystal form of the diclofenac salt on the surface is fine, and the granule surface is smooth with no irregularities. It also handles well,
Moreover, it has the feature that there is little variation in the amount of drug contained in each granule.

すなわち、本発明は、ジクロフェナク塩と結合剤を小粒
状核に被覆してなるジクロフェナク塩粒状顆粒、並びに
、ジクロフェナク塩と結合剤を水−有機溶媒に溶解し、
この溶液を小粒状核に噴霧被覆するジクロフェナク塩粒
状顧粒の製造法に関するものである。
That is, the present invention provides diclofenac salt granules in which small granular cores are coated with diclofenac salt and a binder, as well as diclofenac salt and binder dissolved in a water-organic solvent,
The present invention relates to a method for producing diclofenac salt granules by spraying this solution onto small granular cores.

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

まず、本発明において、「ジクロフェナク塩」とは、ジ
クロフェナクナトリウム、ジクロフェナクカリウム、ジ
クロフェナクアンモニウム、ジクロツェナフカルシウム
、ジクロフェナクアルミニウム等の無機塩、並びにジク
ロツェナクジメチルアミノエタノール、ジクロフェナク
トリメチルアミン等の有機塩をいう。
First, in the present invention, "diclofenac salt" refers to inorganic salts such as diclofenac sodium, diclofenac potassium, diclofenac ammonium, diclozenaf calcium, and diclofenac aluminum, and organic salts such as diclozenac dimethylaminoethanol and diclofenac trimethylamine. .

本発明において、粒状顆粒の核となる「小粒状核」は、
精製白糖、精製白糖−コーンスターチ混合物等により製
造した粒径0.1〜3 mm程度の小粒物である。かか
る例としては、ノンバレル(商品名、フロイント産業(
11社製)が好適に使用可能である。
In the present invention, the "small granular nucleus" that is the core of the granular granule is
It is a small particle with a particle size of about 0.1 to 3 mm manufactured from refined white sugar, a refined white sugar-cornstarch mixture, etc. Such examples include Nonbarrel (trade name, Freund Sangyo (trade name)).
(manufactured by 11 companies) can be suitably used.

本発明における「結合剤」としては、水溶性高分子、p
)I依存性高分子、水不溶性高分子の1種又は2種以上
の混合物が用いられる。前記水溶性高分子の例としては
、ヒドロキシプロピルメチルセルロース、ヒドロキシプ
ロピルセルロース、ポリビニルピロリドン、メチルセル
ロース、等カ挙ケラれる。またpH依存性高分子の例と
しては、例えば、ヒドロキシプロピルメチルセルロース
フタレート、オイドラギット し又はS(商品名、ロー
ム・アンド・ハース社製、成分ニアクリル酸−メタクリ
ル酸エステル共重合体)、カルボキシメチルエチルセル
ロース等が、また水不溶性高分子の例として、オイドラ
ギット RL又はR3(商品名、ローム・アンド・ハー
ス社製、成分ニアクリル酸−メタクリル酸エステル共重
合体)、エチルセルロース等が挙げられる。
The "binder" in the present invention includes a water-soluble polymer, p
) One or a mixture of two or more of I-dependent polymers and water-insoluble polymers can be used. Examples of the water-soluble polymer include hydroxypropylmethylcellulose, hydroxypropylcellulose, polyvinylpyrrolidone, methylcellulose, and the like. Examples of pH-dependent polymers include hydroxypropyl methylcellulose phthalate, Eudragit Shika S (trade name, manufactured by Rohm and Haas, component nialic acid-methacrylic acid ester copolymer), carboxymethyl ethyl cellulose, etc. However, examples of water-insoluble polymers include Eudragit RL or R3 (trade name, manufactured by Rohm and Haas, component: nialic acid-methacrylic acid ester copolymer), ethyl cellulose, and the like.

これらの高分子は、単独又はそれらを混合して用いる。These polymers may be used alone or in combination.

好適には、ポリビニルピロリドン、エチルセルロース、
オイドラギット RL又はR3を用いると良好な結果が
得られる。
Preferably, polyvinylpyrrolidone, ethylcellulose,
Good results are obtained using Eudragit RL or R3.

本発明において、「水−有機溶媒の混合溶媒」としては
、水−エタノール、水−エタノール−アセトンの混合溶
媒が好適に用いろる。なおりロロホルム、ジクロロメタ
ン等のハロゲン系有機溶媒は排気による環境汚染、溶媒
残留等の点でその使用は好ましくない。前記において例
えば水−エタノールの混合割合は、容積比で水−エタノ
ール5;95〜3;7の範囲が好ましい。特に約1:9
の混合割合が好適である。
In the present invention, as the "water-organic solvent mixed solvent", water-ethanol and water-ethanol-acetone mixed solvents are preferably used. Furthermore, the use of halogenated organic solvents such as loloform and dichloromethane is undesirable in view of environmental pollution due to exhaust gas, solvent residue, and the like. In the above, for example, the mixing ratio of water and ethanol is preferably in the range of 5:95 to 3:7 by volume. Especially about 1:9
A mixing ratio of is suitable.

この混合溶媒の混合割合によるジクロフェナクナトリウ
ムの溶解度を第1図に示した。
Figure 1 shows the solubility of diclofenac sodium depending on the mixing ratio of this mixed solvent.

次に本発明の粒状顆粒の製造法につき、以下例示する。Next, the method for producing the granules of the present invention will be exemplified below.

まず、ジクロフェナク塩と前述の結合剤を、水−を機溶
媒に溶解する。結合剤の濃度は、使用する結合剤の種類
によって異なるが、普通0.1〜5%(重量比)の範囲
、特に0.3〜1.0%の範囲が好適である。この範囲
では、粉の飛散や顆粒同士の付着による団粒生成は全く
みられず、タルク等の滑沢剤の添加を必要とせず、それ
故被覆が容易である。
First, diclofenac salt and the above-mentioned binder are dissolved in a water-based organic solvent. The concentration of the binder varies depending on the type of binder used, but is generally in the range of 0.1 to 5% (weight ratio), particularly preferably in the range of 0.3 to 1.0%. Within this range, no agglomerate formation due to scattering of powder or adhesion of granules to each other is observed, no addition of a lubricant such as talc is required, and therefore coating is easy.

また、ジクロフェナク塩の濃度は、1%〜30%(重量
比)の範囲、特に10〜20%の範囲が好適である。こ
の範囲の濃度では、環境温度が比較的低いときでも、ジ
クロフェナク塩の結晶析出がなく、そのため溶液を加温
しなくともよいという利点がある。
The concentration of diclofenac salt is preferably in the range of 1% to 30% (weight ratio), particularly in the range of 10 to 20%. Concentrations in this range have the advantage that there is no crystal precipitation of diclofenac salt even when the environmental temperature is relatively low, so there is no need to heat the solution.

尚、上記ジクロフェナク塩と結合剤の溶液を小粒状核に
被覆する方法としては、噴霧被覆法が適用される。
Incidentally, as a method for coating the small granular cores with the solution of the diclofenac salt and binder, a spray coating method is applied.

以上の如くして得られた、小粒成核にジクロフェナク塩
を被覆した粒状顆粒のその表面に、さらに徐放性膜によ
る被覆、腸溶性膜による被覆などを行って、連続した多
層被覆体とすることも出来る。この場合、従来の粉末コ
ート法ではコーティング層内の粉末の飛散が著しく、2
工程と工程数が増えるのに比べ、溶液コート法では、コ
ーティング層内の粉末の飛散はほとんどなく、連続して
多層コーティングが可能であるという特長を有する。
The surface of the granules obtained as above, in which the small nucleated particles are coated with diclofenac salt, is further coated with a sustained-release film, an enteric film, etc. to form a continuous multilayer coated body. You can also do that. In this case, in the conventional powder coating method, the powder within the coating layer scatters significantly, and
While the number of steps and processes increases, the solution coating method has the advantage that there is almost no scattering of powder within the coating layer, and continuous multilayer coating is possible.

以下、本発明の粒状顆粒の製造法を、実施例をもって説
明する。
Hereinafter, the method for producing granules of the present invention will be explained with reference to Examples.

〔実施例〕〔Example〕

実施例1 ノンバレル 103(商品名、フロイント産業(#@社
製、成分:精製白P)1kgを、遠心流動装置に入れ、
これにジクロフェナクナトリウム300g、ポリビニル
ピロリドン K−904,5gを水・エタノール溶液(
1:9、v / v ) 1500mf!に完全に溶解
した液を、常法により噴霧し、40℃で16時間乾燥し
て粒状顆粒を得た。
Example 1 1 kg of Non-Barrel 103 (trade name, manufactured by Freund Sangyo (#@ company, ingredient: purified white P) was placed in a centrifugal flow device,
To this, 300 g of diclofenac sodium and 5 g of polyvinylpyrrolidone K-904 were added in a water/ethanol solution (
1:9, v/v) 1500mf! A completely dissolved solution was sprayed by a conventional method and dried at 40° C. for 16 hours to obtain granules.

実施例2 ポリビニルピロリドン K−90の代わりに、エチルセ
ルロースを用い、実施例1と同1・玉に操1乍して粒状
顆粒を得た。
Example 2 Ethylcellulose was used instead of polyvinylpyrrolidone K-90, and the same procedure as in Example 1 was carried out to obtain granules.

実施例3 ポリビニルピロリドン K−90の代わりに、オイドラ
ギット R3−100(商品名、ローム・アンド・ハー
ス社製、成分ニアクリル酸−メタクリル酸メチル共重合
体)を用い、実施例1と同様に操作して粒状顆粒を得た
Example 3 The procedure was repeated in the same manner as in Example 1, using Eudragit R3-100 (trade name, manufactured by Rohm and Haas, component: niacryl acid-methyl methacrylate copolymer) instead of polyvinylpyrrolidone K-90. Granular granules were obtained.

実施例4 ポリビニルピロリドン K−90の代わりに、HP−5
5(商品名、信越化学工業(l菊社製、成分:ヒドロキ
シプロピルメチルセルロースフタレート)を用い、実施
例1と同様に操作し、て粒状顆粒を得た。
Example 4 HP-5 instead of polyvinylpyrrolidone K-90
5 (trade name, manufactured by Shin-Etsu Chemical Co., Ltd. (l Kikusha, component: hydroxypropyl methyl cellulose phthalate)) and operated in the same manner as in Example 1 to obtain granules.

実施例5 ノンバレル 1032.5kgを遠心流!ll装置に入
れ、これにジクロフェナクナトリウム 750g1ポリ
ビニルピロリドン K−9011,25gを水・エタノ
ール溶液(1:9、v/v)375 Qmj!に完全に
溶解した液を常法により噴霧し粒状顆粒を得た。これに
、さらに、ポリビニルピロリドン K−3025gをエ
タノール25〇−に完全に溶解した液を、常法により噴
霧した。
Example 5 Non-barrel 1032.5kg centrifugal flow! 1 750 g of diclofenac sodium 1 25 g of polyvinylpyrrolidone K-9011 in a water/ethanol solution (1:9, v/v) 375 Qmj! A completely dissolved solution was sprayed using a conventional method to obtain granules. Further, a solution prepared by completely dissolving 3025 g of polyvinylpyrrolidone K in 250 g of ethanol was sprayed onto this in a conventional manner.

その際タルク等を添加し、顆粒同士の付着を防いだ。こ
の顆粒をさらに40℃で乾燥して所望の粒状顆粒を得た
At that time, talc or the like was added to prevent the granules from adhering to each other. The granules were further dried at 40°C to obtain desired granules.

実施例6 ノンバレル 1031kgを遠心流動装置に入れ、これ
にジクロフェナクナトリウム 300g。
Example 6 1031 kg of non-barrel was placed in a centrifugal flow device, and 300 g of diclofenac sodium was added thereto.

オイドラギット R3−100100gを水・エタノー
ル・アセトン溶液(2:10:9、V/V)1600m
f!に完全に溶解した液を常法により噴霧し、40℃で
乾燥して所望の粒状顆粒を得た。
Eudragit R3-100 100g in water/ethanol/acetone solution (2:10:9, V/V) 1600m
f! A completely dissolved solution was sprayed in a conventional manner and dried at 40°C to obtain desired granules.

実施例7 ノンバレル 103 2.5 kgを遠心流動装置に入
れ、これにジクロフェナクナトリウム 750g、ポリ
ビニルピロリドン K−9011,25gを水・エタノ
ール溶液(1:9、v/v)3750−に完全に溶解し
た液を常法により噴霧し粒状顆粒を得た。これに、さら
にポリビニルピロリドン K−3025gを水・エタノ
ール(6液(1:9、V/V)250mi!に完全に溶
解した液を、噴霧した。それにエチルセルロース128
g5TC−5R(商品名、信越化学工業(4)社製、成
分:ヒドロキシプロピルメチルセルロース)32g1ク
工ン酸トリエチル8gを水・エタノール溶液(5: 9
5v/v)3200mlに完全に溶解した液を、さらに
噴霧した。その際タルクを添加し顆粒同士の付着を防い
だ。この顆粒を40℃で乾燥して所望の除放性粒状顆粒
を得た。
Example 7 2.5 kg of Nonbarrel 103 was placed in a centrifugal flow device, and 750 g of diclofenac sodium and 25 g of polyvinylpyrrolidone K-9011 were completely dissolved in a water/ethanol solution (1:9, v/v) of 3750. The liquid was sprayed in a conventional manner to obtain granules. This was further sprayed with a solution in which 25 g of polyvinylpyrrolidone K-30 was completely dissolved in water/ethanol (6 liquids (1:9, V/V) 250 ml!). Ethyl cellulose 128
g5TC-5R (trade name, manufactured by Shin-Etsu Chemical Co., Ltd. (4), ingredients: hydroxypropyl methylcellulose) 32g1 8g of triethyl citrate in a water/ethanol solution (5:9)
The solution completely dissolved in 3200 ml of 5v/v) was further sprayed. At that time, talc was added to prevent the granules from adhering to each other. The granules were dried at 40°C to obtain desired sustained release granules.

実施例8 ノンバレル 1031kgを遠心流動装置に入れ、これ
にジクロフェナクナトリウム 300 g。
Example 8 1031 kg of non-barrel was placed in a centrifugal flow device, and 300 g of diclofenac sodium was added thereto.

オイドラギット R3−1004,5gを水・エタノー
ル溶液(1:9、v/v)15001T11!に完全に
溶解した液を常法により噴霧し粒状顆粒を僻だ。これに
さらに、オイドラギット R3−100100g、クエ
ン酸トリエチル 10gを水・エタノール溶液(5:9
5、v/v)1000mffiに完全に溶解した液を、
常法により噴霧した。その際タルクを添加し顆粒同士の
付着を防いだ。この粕粒を40℃で乾燥して所望の除放
性粒状顆粒を得た。
Eudragit R3-1004, 5g in water/ethanol solution (1:9, v/v) 15001T11! A completely dissolved solution is sprayed using a conventional method to remove granules. In addition, 100 g of Eudragit R3-100 and 10 g of triethyl citrate were added in a water/ethanol solution (5:9
5.v/v) The solution completely dissolved in 1000mffi,
It was sprayed using a conventional method. At that time, talc was added to prevent the granules from adhering to each other. This lees was dried at 40°C to obtain desired sustained release granules.

実施例9 ノンバレル 1031kgを遠心流動装置に入れ、これ
にジクロフェナクナトリウム 300g。
Example 9 1031 kg of non-barrel was placed in a centrifugal flow device, and 300 g of diclofenac sodium was added thereto.

オイドラギット R3−1004,5gを水・エタノー
ル溶液(1:9、v/v)1500mj!に完全に溶解
した液を常法により噴霧し粒状顆粒を得た。これにさら
に、オイドラギット L−100240g、クエン酸ト
リエチル 24gを水・エタノール溶液(5:95、v
/v) 4000miに完全に溶解した液を、常法によ
り噴霧した。その際タルクを添加し顆粒同士の付着を防
いだ。この顆粒を40℃で乾燥して、所望の腸溶性粒状
顆粒を得た。
Eudragit R3-1004, 5g in water/ethanol solution (1:9, v/v) 1500mj! A completely dissolved solution was sprayed using a conventional method to obtain granules. In addition, 240 g of Eudragit L-100 and 24 g of triethyl citrate were added in a water/ethanol solution (5:95, v.
/v) A solution completely dissolved at 4000 mi was sprayed by a conventional method. At that time, talc was added to prevent the granules from adhering to each other. The granules were dried at 40°C to obtain the desired enteric coated granules.

〔発明の効果〕〔Effect of the invention〕

本発明の小粒状顆粒は、小粒子状核の表面に均一かつ微
細な結晶のジクロフェナク塩が被覆され、その小粒状顆
粒の表面が平滑である。そのため、次の製造工程に対し
て取り扱いが容易である。また粉の飛散等がなく、その
後の製造工程が連続して行える利点がある。
In the small granules of the present invention, the surface of the small core is coated with uniform and fine crystalline diclofenac salt, and the surface of the small granules is smooth. Therefore, it is easy to handle for the next manufacturing process. It also has the advantage that there is no scattering of powder, and subsequent manufacturing steps can be carried out continuously.

また、賦形剤等の粉体を使用しないので、粉体とジクロ
フェナク塩との混合により生ずる篩過・混合・乾燥等の
、煩雑で、しかも時間のかかる操作が省略される。それ
故それに伴う労力、原材料の損失等の多くの難点が解決
され、極めて工業的に優れた効果を有するものであると
いうことができる。
Furthermore, since no powder such as an excipient is used, complicated and time-consuming operations such as sieving, mixing, and drying that occur when the powder and diclofenac salt are mixed are omitted. Therefore, many problems associated with this, such as labor and loss of raw materials, are solved, and it can be said that it has extremely excellent industrial effects.

次に、本発明の粒状顆粒の安定性が従来のものよりも優
れていることを示す試験結果を示す。
Next, test results showing that the stability of the granular granules of the present invention are superior to conventional ones are shown.

安定性試験 本発明のジクロフェナクナトリウム顆粒(実施例1〜3
で得られたもの)と、ジクロフェナクナトリウムと賦形
剤および通常用いられる安定化剤を配合し結合剤で被覆
した粒状顆粒(後記する比較例1〜6で得られたもの)
との経時安定性について比較試験を行った。
Stability test Diclofenac sodium granules of the present invention (Examples 1 to 3)
(obtained in Comparative Examples 1 to 6 described later) and granules prepared by blending diclofenac sodium, excipients, and commonly used stabilizers and coating with a binder (obtained in Comparative Examples 1 to 6 described below)
A comparative test was conducted on stability over time.

比較例1 ジクロフェナクナトリウム 500g、コーンスターチ
 465g、タルク 62gを混合後、篩(145メツ
シユ)にて篩過後、40℃で12時間乾燥した。ノンバ
レル 1031kgを遠心流動装置に入れ、上記粉末を
かけながらポリビニルピロリドン K−90を3%(W
/V)含有する水・エタノール溶液(3:2)700m
lをスプレーし造粒し、さらに40℃で16時間乾燥し
て粒状顆粒を得た。
Comparative Example 1 500 g of diclofenac sodium, 465 g of cornstarch, and 62 g of talc were mixed, passed through a sieve (145 mesh), and dried at 40° C. for 12 hours. Put 1031 kg of non-barrel into a centrifugal flow device, and add 3% (W) of polyvinylpyrrolidone K-90 while applying the above powder.
/V) Containing water/ethanol solution (3:2) 700m
1 was sprayed to granulate the mixture, and the mixture was further dried at 40° C. for 16 hours to obtain granules.

比較例2 ジクロフェナクナトリウム 250g、コーンスターチ
 222g、タルク 30gを混合後、篩(145メツ
シユ)にて篩過後、40℃で12時間乾燥した。ノンバ
レル l O30,5kgを遠心流動装置に入れ、上記
粉末をかけながらポリビニルピロリドン K−90を3
%(W/V) 、エデト酸カルシウムを0.3%(W/
V)含有する水・エタノール溶液(3:2)350mi
!をスプレーし造粒し、さらに40℃で16時間乾燥し
て粒状宋頁粒をi等だ。
Comparative Example 2 250 g of diclofenac sodium, 222 g of corn starch, and 30 g of talc were mixed, passed through a sieve (145 mesh), and dried at 40° C. for 12 hours. Put 30.5 kg of non-barrel l O into a centrifugal flow device, and add 30.5 kg of polyvinylpyrrolidone K-90 while pouring the above powder.
% (W/V), calcium edetate 0.3% (W/V)
V) Containing water/ethanol solution (3:2) 350mi
! The mixture was sprayed and granulated, and further dried at 40°C for 16 hours to obtain granulated Song Pei grains.

比較例3 エデト酸カルシウムの代わりに、亜硫酸水素ナトリウム
を用い、比較例2と同様に操作して粒状顆粒を得た。
Comparative Example 3 Granular granules were obtained in the same manner as in Comparative Example 2, using sodium hydrogen sulfite instead of calcium edetate.

比較例4 エデト酸カルシウムの代わりに、チナ硫酸ナトリウムを
用い、比較例2と同様に操作して粒状顆粒を得た。
Comparative Example 4 Granular granules were obtained in the same manner as in Comparative Example 2, using sodium china sulfate instead of calcium edetate.

比較例5 エデト酸カルシウムの代わりに、L−システィン塩酸塩
を用い、比較例2と同様に操作して粒状顆粒を得た。
Comparative Example 5 Granular granules were obtained in the same manner as in Comparative Example 2, using L-cystine hydrochloride instead of calcium edetate.

比較例6 ジクロフェナクナトリウム 250g、コーンスターチ
 222g、タルク 30g、ブチルヒドロキシトルエ
ン(BHT)Igを混合後、篩(145メツシユ)にて
篩過後、40℃で12時間乾燥した。ノンバレル 10
30.5 kgを遠心流動装置に入れ、上記粉末をかけ
ながら、ポリビニルピロリドン K−90を3%(W/
V)含有する水・エタノール溶液(3:2)350mj
!をスプレーし造、粒し、さらに40℃で16時間乾燥
して粒状顆粒を得た。
Comparative Example 6 After mixing 250 g of diclofenac sodium, 222 g of cornstarch, 30 g of talc, and Ig of butylated hydroxytoluene (BHT), the mixture was passed through a sieve (145 mesh) and dried at 40° C. for 12 hours. Non-barrel 10
30.5 kg was placed in a centrifugal flow device, and while applying the above powder, 3% (W/W) polyvinylpyrrolidone K-90 was added.
V) Containing water/ethanol solution (3:2) 350 mj
! The mixture was sprayed, granulated, and further dried at 40°C for 16 hours to obtain granules.

(安定性試験) 試験は、各頚粒を55℃、相対湿度60%の条件で1ケ
月、または、40℃、相対湿度75%の条件で6ケ月保
存後、着色の観察および液体クロマトグラフィーによる
分解物の分析を行った。
(Stability test) The test was carried out by storing each neck grain for one month at 55°C and 60% relative humidity, or for 6 months at 40°C and 75% relative humidity, and then observing the coloration and using liquid chromatography. The decomposition products were analyzed.

結果は表1の通りであった。The results are shown in Table 1.

この結果より明らかな如く、本発明の粒状顆粒は着色は
ほとんどなく、分解物も認められなかった。、それに比
較して、粉末状態で被覆した粒状頚粒は、淡褐色に着色
し、分解物(2種)が認められた。この分解物は、ジク
ロフェナクの還元生成物であり、[:2− (2,6−
ジクロロアニリノ)ベンズアルデヒド及び、2−(2,
6−ジクロロアニリノ)ベンジルアルコール〕と同定さ
れた。
As is clear from the results, the granules of the present invention had almost no coloration and no decomposition products were observed. In comparison, the granular neck particles coated in powder form were colored pale brown, and decomposition products (2 types) were observed. This decomposition product is a reduction product of diclofenac, [:2- (2,6-
dichloroanilino)benzaldehyde and 2-(2,
6-dichloroanilino)benzyl alcohol].

すなわち、これらはジクロフェナクと結合剤、賦形剤、
滑沢剤等との相互作用に基づく生成物と考えられる。尚
、これらは通常用いられる安定化剤(キレート剤、抗酸
化剤等)を添加してもその生成をさけることができなか
った。
That is, these include diclofenac, binders, excipients,
It is thought to be a product based on interaction with lubricants, etc. Incidentally, their formation could not be avoided even by adding commonly used stabilizers (chelating agents, antioxidants, etc.).

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

第1図は、ジクロフェナクナトリウムの水−エタノール
混合溶媒に対する溶解性を示すものである。 縦軸はジクロフェナクナトリウム1gを溶かすのに必要
な溶媒量(mりを対数目盛で示し、また横軸は水とエタ
ノールとの溶媒組成比を示す。 第1図 水0%  50%  100%
FIG. 1 shows the solubility of diclofenac sodium in a water-ethanol mixed solvent. The vertical axis shows the amount of solvent (millimeter) required to dissolve 1 g of diclofenac sodium on a logarithmic scale, and the horizontal axis shows the solvent composition ratio of water and ethanol. Figure 1 Water 0% 50% 100%

Claims (6)

【特許請求の範囲】[Claims] (1)ジクロフェナク塩と結合剤とを、小粒状核の表面
に均一に被覆してなることを特徴とするジクロフェナク
塩の粒状組成物。
(1) A granular composition of diclofenac salt, characterized in that the surface of small granular cores is uniformly coated with diclofenac salt and a binder.
(2)ジクロフェナク塩がジクロフェナクナトリウムで
ある特許請求の範囲第(1)項記載のジクロフェナク塩
の粒状組成物。
(2) The granular composition of diclofenac salt according to claim (1), wherein the diclofenac salt is diclofenac sodium.
(3)ジクロフェナク塩と結合剤とを、水−有機溶媒の
混合溶液に溶解し、この溶液を小粒状核に噴霧すること
を特徴とするジクロフェナク塩の粒状組成物の製造法。
(3) A method for producing a granular composition of diclofenac salt, which comprises dissolving diclofenac salt and a binder in a mixed solution of water and an organic solvent, and spraying this solution onto small granular nuclei.
(4)有機溶媒がエタノールである特許請求の範囲第(
3)項記載のジクロフェナク塩の粒状組成物の製造法。
(4) Claim No. 1 in which the organic solvent is ethanol (
3) A method for producing a granular composition of diclofenac salt according to item 3).
(5)水−有機溶媒の混合溶媒が、水−エタノール=1
:9(容積比)である特許請求の範囲第(3)項記載の
ジクロフェナク塩の粒状組成物の製造法。
(5) The mixed solvent of water and organic solvent is water-ethanol=1
:9 (volume ratio).
(6)ジクロフェナク塩が、ジクロフェナクナトリウム
である特許請求の範囲第(3)項記載のジクロフェナク
塩の粒状組成物の製造法。
(6) The method for producing a granular composition of diclofenac salt according to claim (3), wherein the diclofenac salt is diclofenac sodium.
JP27478585A 1985-12-06 1985-12-06 Granular composition of diclofenac salt and production thereof Pending JPS62135419A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP27478585A JPS62135419A (en) 1985-12-06 1985-12-06 Granular composition of diclofenac salt and production thereof

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP27478585A JPS62135419A (en) 1985-12-06 1985-12-06 Granular composition of diclofenac salt and production thereof

Publications (1)

Publication Number Publication Date
JPS62135419A true JPS62135419A (en) 1987-06-18

Family

ID=17546525

Family Applications (1)

Application Number Title Priority Date Filing Date
JP27478585A Pending JPS62135419A (en) 1985-12-06 1985-12-06 Granular composition of diclofenac salt and production thereof

Country Status (1)

Country Link
JP (1) JPS62135419A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5800836A (en) * 1992-08-05 1998-09-01 F. H. Faulding & Co. Limited Pelletized pharmaceutical composition
WO2004105725A3 (en) * 2003-05-30 2005-05-26 Eurand Spa Microcapsules by coacervation containing a pharmaceutical incorporated in the coating polymer
WO2005048731A3 (en) * 2003-11-17 2005-09-15 Cargill Inc Lecithin-containing granular compositions and methods of their preparation

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5800836A (en) * 1992-08-05 1998-09-01 F. H. Faulding & Co. Limited Pelletized pharmaceutical composition
WO2004105725A3 (en) * 2003-05-30 2005-05-26 Eurand Spa Microcapsules by coacervation containing a pharmaceutical incorporated in the coating polymer
JP2007509844A (en) * 2003-05-30 2007-04-19 ユーランド ソシエタ ペル アチオニ Microcapsules with drug introduced into coating polymer by coacervation
WO2005048731A3 (en) * 2003-11-17 2005-09-15 Cargill Inc Lecithin-containing granular compositions and methods of their preparation

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