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JPH0532373B2 - - Google Patents
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JPH0532373B2 - - Google Patents

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Publication number
JPH0532373B2
JPH0532373B2 JP58042722A JP4272283A JPH0532373B2 JP H0532373 B2 JPH0532373 B2 JP H0532373B2 JP 58042722 A JP58042722 A JP 58042722A JP 4272283 A JP4272283 A JP 4272283A JP H0532373 B2 JPH0532373 B2 JP H0532373B2
Authority
JP
Japan
Prior art keywords
disintegrant
mesh
particle size
fine powder
cellulose
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.)
Expired - Lifetime
Application number
JP58042722A
Other languages
Japanese (ja)
Other versions
JPS59167522A (en
Inventor
Takahiro Koyama
Haruo Matsumura
Tetsuo Morita
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.)
Nichirin Chemical Industries Ltd
Original Assignee
Nichirin 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 Nichirin Chemical Industries Ltd filed Critical Nichirin Chemical Industries Ltd
Priority to JP4272283A priority Critical patent/JPS59167522A/en
Priority to KR1019840000850A priority patent/KR840007590A/en
Publication of JPS59167522A publication Critical patent/JPS59167522A/en
Publication of JPH0532373B2 publication Critical patent/JPH0532373B2/ja
Granted legal-status Critical Current

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  • Medicinal Preparation (AREA)

Description

【発明の詳細な説明】[Detailed description of the invention]

この発明は崩壊性の改良された固型薬剤の製法
に関するものであり、詳しくは特定の粒度の崩壊
剤を選択使用することにより性能の改良された固
型薬剤の製造する方法に関するものである。 固型薬剤とは流通、保存、取扱ならびに服用に
便利なように薬効成分に賦型剤、結合剤、崩壊
剤、滑沢剤などを添加し、混和成形して錠剤、丸
剤、顆粒剤などの形態としたものである。 上記配合成分の中で、崩壊剤とは人体の消化液
中で容易に崩壊する性能を固型薬剤に与えるため
のものであり、経口摂取後、消火器官内で薬効成
分が速やかに放出されるようにするためのもので
ある。 上記の崩壊剤には、澱粉、ホルマール化ゼラチ
ン、アルギン酸、繊維素グリコール酸(遊離酸)、
繊維素グリコール酸カルシウム、低置換度アルキ
ル繊維素、低置換度ヒドロキシアルキル繊維素な
どが提案されており、数種類のものが実用に供さ
れている。なかでも繊維素グリコール酸カルシウ
ムは無味、無臭、白色であること、崩壊性が良く
膨潤倍率が大であり、圧縮成形性があることなど
最も優れた性能を有するものと認められており最
も大量に使用されている。 しかしながら、繊維素グリコール酸カルシウム
についても、結合性に乏しいため、多量に使用す
ると成形薬剤の硬度が不足すること、水中での崩
壊は速くても、胃液中の崩壊速度は必ずしもそれ
ほど大きくないことなどが指摘されている。 現在市販され、工業的に使用されている繊維素
グリコール酸カルシウムは、ECG−505の商標の
もとに製造販売されている単一グレードのみであ
り、その標準物性、分析値として、無水グルコー
ス単位の重合度約300、カルボキシメチル基置換
度0.6、水中に1重量%を分散懸濁させたときの
媒体のPHは約5、95重量部以上が200メツシユ通
過の粒度を有するものである。 発明者等はこれに対し、実際の固型薬剤への使
用に当つては、繊維素グリコース酸カルシウムの
微粉末留分をなくし特定の粒度以上に限つたもの
が、現在市販のものよりも優れた崩壊性を有する
ものであることを見出した。固型薬剤の製造に当
つては、その配合成分ができるだけ均一な混合状
態にあることが望ましく、そのためには配合成分
の粒度は一般に細かい方が良いと考えられてき
た。特に繊維素グリコール酸カルシウムの場合、
配合量はせいぜい全体の2〜10重量%程度である
ため粒度は細かくして使用するのが一般的であつ
た。即ち諸規格においても粒子の上限のみが定め
られ微粉末留分の存在には留意されなかつた。 例えば繊維素グリコール酸カルシウムの製造特
許である特公昭43−7960明細書において実施例1
では200メツシユに粉砕したもの、実施例2では
150メツシユに粉砕したものをそれぞれ製品とし
ている。これらは製品粒度上限の大きさがそれぞ
れ200メツシユおよび150メツシユであり、それら
に相当する篩の目を通過するものは全部含むとい
うことである。何故ならば粉砕によつて粒子を得
る場合、常に微粉末留分を伴うからである。発明
者等は、繊維素グリコール酸を炭酸カルシウムを
用いて中和し、粉砕して得た繊維素グリコール酸
カルシウムを篩分し、粒度の異なるものを調製し
これを配合した固型薬剤を成型しそれらの崩壊性
を調べた結果、微粉末留分を含有しない繊維素グ
リコール酸カルシウムを用いたものが微粉末留分
を含有する場合に比べて崩壊性に優れたものであ
ることを見出した。 発明者等の考察によれば、繊維素グリコール酸
カルシウムの崩壊剤としての特徴は、水系媒体中
での膨潤倍率の大きいことであり、崩壊剤が先づ
媒体を吸収して膨潤し、固型薬剤内部に応力を与
え全体を崩壊に導くのである。このような機構で
崩壊を起こるとすれば、個々の崩壊剤粒子はある
程度の大きさに集まつている方が効果的に応力を
働かすことができる。微粉末留分は、それが膨潤
してもその圧力は周囲の他成分粒子に吸収されて
しまい効果が充分発揮されないことが考えられ
る。このことは、崩壊剤の配合量がせいぜい5重
量%程度の少量であることを考慮しなければなら
ない。微粉末留分を含有することはその分だけ崩
壊剤としての効果の低い留分を含有することにな
る。 この発明の発明者等の検討によれば粒度80メツ
シユ以下の場合、繊維素グリコール酸カルシウム
の粒度は大きい方が崩壊性に優れた固型薬剤が得
られることを認めた。しかし、粒度の大きいもの
は製剤の硬度が相対的に低下する傾向も見出され
た。これは繊維素グリコール酸カルシウムが結合
性についての機能が低いことで説明される。 即ちこの発明は、微粉末留分を含まない繊維素
グリコール酸カルシウムを崩壊剤として使用する
ことを特徴とする固型薬剤の製法に関するもので
ある。具体的には“微粉末留分を含まない”崩壊
剤として“300メツシユ 通過分を含まない”崩
壊剤を使用すれば、崩壊性に優れた固型薬剤が得
られる。但し、崩壊剤の粒度が大きくなると固型
薬剤の硬度が低下する傾向にあるので硬度、崩壊
性の両性能を満足させる崩壊剤としては145メツ
シユ通過、300メツシユ不通過の繊維素グリコー
ル酸カルシウムを使用するのが好ましい。 本発明において使用する繊維素グリコール酸カ
ルシウムは、無水グルコース単位あたりのカルボ
キシメチル置換度、即ちエーテル化度は0.30以上
0.80以下が適当である。エーテル化度が0.3以下
では崩壊性、膨潤倍率が充分でなく、0.85以上で
は崩壊性が特に良くはならないのに固型薬剤の硬
度が低下する傾向がある。 以下に実施例を挙げて本発明を説明する。 実施例1〜2及び比較例1〜3 無水グルコース単位あたりのカルボキシメチル
基置換度0.53、中和度PH5.2の繊維素グリコール
酸カルシウムを次のように篩分した。 崩壊剤粒度 145メツシユ通過〜200メツシユ不通過 b 200メツシユ〃 〜300メツシユ 〃 c 80メツシユ〃 〜145メツシユ 〃 d 200メツシユ〃 (微粉含有)規格品 e 300メツシユ〃 (微粉含有) 上記繊維素グリコール酸カルシウムを崩壊剤と
して使用し、薬効成分としてアスコルビン酸、賦
形剤として微結晶セルロース(アビセルPH101旭
化成製)及び乳糖、滑沢剤としてタルク及びステ
アリン酸マグネシウムを配合した錠剤を直接打錠
法によつて作製した。 錠剤組成及び製剤条件は次の通りである。 錠剤組成: アスコルビン酸 50.0重量% アビセルPH101 28.0 〃 乳 糖 14.0 〃 崩壊剤 5.0 〃 タルク 2.5 〃 ステアリン酸マグネシウム 0.5 〃 100.0重量% 製造条件: 打錠機 菊水製作所製クリーンプレスコレクト24 成型条件 錠径8mmφ、錠剤厚み4mm、重量200
mg、打錠圧1t 錠剤物性は次の方向で測定した。 崩壊性 日本薬局方準拠崩壊度試験機(富山産業
株式会社) 測定温度 37±2℃ 試験液 局方第1液(人工胃液) n=10、崩壊に要した時間の平均値(秒)で
示す 硬 度 試験機 テンシロンUTM−1(東洋精
機) 圧縮ロードセル 100Kg/cm2 圧縮荷重機直径2.0mm 圧縮速度 0.4mm/min n=8、破壊がはじまる直前の圧力の平均値で
示す(Kg/cm2) 磨損度 萱坦式磨損度試験機 25回転 3分間処理 100個の錠剤を処理し、粉末化した部分の重量
を百分率(%)で示す 使用した崩壊剤の粒度と錠剤物性を第1表に示
The present invention relates to a method for producing a solid drug with improved disintegrability, and more particularly, to a method for producing a solid drug with improved performance by selectively using a disintegrant with a specific particle size. Solid drugs are tablets, pills, granules, etc. that are mixed and molded with excipients, binders, disintegrants, lubricants, etc. added to the medicinal ingredients for convenient distribution, storage, handling, and administration. It is in the form of Among the above compounded ingredients, disintegrants are used to give solid drugs the ability to easily disintegrate in the human body's digestive fluids, and after oral ingestion, the medicinal ingredients are quickly released in the fire extinguishing organs. It is intended to do so. The disintegrants mentioned above include starch, formalized gelatin, alginic acid, cellulose glycolic acid (free acid),
Cellulose calcium glycolate, low-substituted alkyl cellulose, low-substituted hydroxyalkyl cellulose, and the like have been proposed, and several types are in practical use. Among them, cellulose calcium glycolate is recognized as having the best performance such as being tasteless, odorless, and white, having good disintegration properties, high swelling ratio, and compression moldability, and is used in the largest quantities. It is used. However, calcium fibrin glycolate also has poor binding properties, so if used in large quantities, the hardness of the molding agent will be insufficient, and even though it disintegrates quickly in water, the rate of disintegration in gastric fluid is not necessarily that high. has been pointed out. The cellulose calcium glycolate that is currently commercially available and used industrially is only a single grade manufactured and sold under the trademark ECG-505, and its standard physical properties and analytical values are based on anhydroglucose units. The polymerization degree is about 300, the carboxymethyl group substitution degree is 0.6, the pH of the medium when 1% by weight is dispersed and suspended in water is about 5, and the particle size is such that 95 parts by weight or more can pass through 200 meshes. In contrast, the inventors believe that, when used in actual solid drugs, a product that eliminates the fine powder fraction of cellulose calcium glycolate and is limited to a specific particle size or more is superior to products currently on the market. It was found that the material had a disintegrating property. When producing a solid drug, it is desirable that the ingredients are mixed as uniformly as possible, and for this purpose it has generally been thought that the finer the particle size of the ingredients, the better. Especially in the case of cellulose calcium glycolate,
Since the blending amount is at most about 2 to 10% by weight of the total, it has generally been used with fine particle size. That is, in various standards, only the upper limit of particles was determined, and no consideration was given to the existence of fine powder fractions. For example, in the specification of Japanese Patent Publication No. 43-7960, which is a manufacturing patent for cellulose calcium glycolate, Example 1
In Example 2, it was ground into 200 mesh pieces.
Each product is made by crushing it into 150 pieces. The upper limit particle size of these products is 200 mesh and 150 mesh, respectively, and all particles that can pass through a sieve corresponding to these sizes are included. This is because when particles are obtained by grinding, a fine powder fraction is always accompanied. The inventors neutralized cellulose glycolic acid using calcium carbonate, sieved the obtained cellulose glycolic acid calcium by pulverization, prepared particles with different particle sizes, and molded the solid drug by blending the same. As a result of investigating their disintegration properties, it was found that those using cellulose calcium glycolate that did not contain fine powder fractions had superior disintegration properties compared to those containing fine powder fractions. . According to the inventors' considerations, the characteristic of cellulose calcium glycolate as a disintegrant is that it has a large swelling ratio in an aqueous medium, and the disintegrant first absorbs the medium and swells, forming a solid This applies stress to the inside of the drug, leading to its collapse. If disintegration occurs through such a mechanism, stress can be applied more effectively if the individual disintegrant particles are gathered to a certain size. It is thought that even if the fine powder fraction swells, the pressure will be absorbed by the surrounding particles of other components and the effect will not be sufficiently exerted. This must be taken into account that the amount of the disintegrant is as small as 5% by weight at most. Containing a fine powder fraction means containing a fraction that is less effective as a disintegrant. According to studies conducted by the inventors of the present invention, it has been found that when the particle size is 80 mesh or less, the larger the particle size of cellulose calcium glycolate, the better a solid drug can be obtained with excellent disintegration properties. However, it was also found that the hardness of the preparation tends to be relatively lower when the particle size is large. This is explained by the poor binding function of fibrin calcium glycolate. That is, the present invention relates to a method for producing a solid drug characterized by using cellulose calcium glycolate containing no fine powder fraction as a disintegrant. Specifically, if a disintegrant that does not contain a fine powder fraction and does not contain a fraction passing through 300 meshes is used, a solid drug with excellent disintegration properties can be obtained. However, as the particle size of the disintegrant increases, the hardness of the solid drug tends to decrease, so as a disintegrant that satisfies both hardness and disintegration properties, use cellulose calcium glycolate that passes 145 mesh but does not pass 300 mesh. It is preferable to use The cellulose calcium glycolate used in the present invention has a degree of carboxymethyl substitution per anhydroglucose unit, that is, a degree of etherification of 0.30 or more.
0.80 or less is appropriate. If the degree of etherification is less than 0.3, the disintegrability and swelling ratio will not be sufficient, and if the degree of etherification is greater than 0.85, the hardness of the solid drug will tend to decrease although the disintegrability will not be particularly good. The present invention will be explained below with reference to Examples. Examples 1 to 2 and Comparative Examples 1 to 3 Cellulose calcium glycolate having a degree of carboxymethyl group substitution per anhydroglucose unit of 0.53 and a degree of neutralization of PH 5.2 was sieved as follows. Disintegrant particle size 145 mesh - 200 mesh does not pass b 200 mesh - 300 mesh c 80 mesh - 145 mesh d 200 mesh (contains fine powder) Standard product e 300 mesh (contains fine powder) Above cellulose glycolic acid A tablet containing calcium as a disintegrant, ascorbic acid as a medicinal ingredient, microcrystalline cellulose (Avicel PH101 manufactured by Asahi Kasei) and lactose as excipients, and talc and magnesium stearate as a lubricant is made by direct compression. I made it using the same method. The tablet composition and formulation conditions are as follows. Tablet composition: Ascorbic acid 50.0% by weight Avicel PH101 28.0 〃 Lactose 14.0 〃 Disintegrant 5.0 〃 Talc 2.5 〃 Magnesium stearate 0.5 〃 100.0% by weight Manufacturing conditions: Tablet press Kikusui Seisakusho Clean Press Collect 24 Molding conditions Tablet diameter 8 mmφ, Tablet thickness: 4mm, weight: 200
mg, tableting pressure 1t Tablet physical properties were measured in the following directions. Disintegration Disintegration tester according to the Japanese Pharmacopoeia (Toyama Sangyo Co., Ltd.) Measurement temperature 37±2℃ Test liquid Pharmacopoeia 1st fluid (artificial gastric fluid) n=10, expressed as the average value (seconds) of the time required for disintegration Hardness tester Tensilon UTM-1 (Toyo Seiki) Compression load cell 100Kg/cm 2 Compression loader diameter 2.0mm Compression speed 0.4mm/min n=8, expressed as the average value of the pressure just before fracture starts (Kg/cm 2 ) Abrasion degree 100 tablets were processed using a Kayadan type abrasion tester for 25 rotations for 3 minutes, and the weight of the powdered portion is shown in percentage (%). The particle size of the disintegrant used and the physical properties of the tablets are shown in Table 1. show

【表】 微粉末留分を含まない崩壊剤を使用した実施例
は、微粉末留分を含む崩壊剤を使用した比較例
(局方規格品を含む)に比べ優れた崩壊性を示し
た。また硬度は粒度の小さい崩壊剤を用いたもの
が高いという傾向を示した。 尚打錠時のキヤツピングは100打錠当り比較例
2は4個、比較例3は1個発生したが実施例1〜
2および比較例1では全く発生しなかつた。 実施例3〜6及び比較例4〜9 実施例1〜2、比較例1〜3に用いたものと同
じ崩壊剤を用い、打錠条件をかえてアスコルビン
酸を主薬とする錠剤及び乳糖を主体とする模擬錠
剤を直接打錠法によつて作製し得られた錠剤につ
き物性を測定した。 錠剤組成: ビタミンC錠:実施例1〜2に同じ組成 模擬錠剤: 乳 糖 93.5重量% 崩壊剤 5.0 〃 タルク 1.0 〃 ステアリン酸マグネシウム 0.5重量% 100.0重量% 打錠条件:錠剤組成物0.70gを12mmφの杆を用い
厚さ4mmの錠剤に成型 崩壊性:35mmφ×2mの管中に局方第一液(人工
胃液37℃)を満し、液面から錠剤を落して液中
に落下させ、完全に分散するのに要する時間を
測定、n=5 硬 度:モンサント硬度計を用いて測定、n=5
測定結果を第2表〜第3表に示す
[Table] Examples using a disintegrant not containing a fine powder fraction showed superior disintegration properties compared to comparative examples (including pharmacopeia standard products) using a disintegrant containing a fine powder fraction. Furthermore, the hardness tended to be higher in those using disintegrants with smaller particle sizes. Incidentally, capping occurred during tablet compression: 4 cappings occurred in Comparative Example 2 and 1 capping occurred in Comparative Example 3 per 100 tablets, but in Examples 1-
In Comparative Example 2 and Comparative Example 1, it did not occur at all. Examples 3 to 6 and Comparative Examples 4 to 9 Using the same disintegrant as that used in Examples 1 to 2 and Comparative Examples 1 to 3, and changing the tableting conditions, tablets containing ascorbic acid as the main drug and lactose as the main drug were prepared. A simulated tablet was prepared using a direct compression method, and the physical properties of the resulting tablet were measured. Tablet composition: Vitamin C tablet: Same composition as Examples 1 and 2 Simulated tablet: Lactose 93.5% by weight Disintegrant 5.0 Talc 1.0 Magnesium stearate 0.5% by weight 100.0% by weight Tableting conditions: 0.70 g of tablet composition was compressed into 12 mmφ Molding into tablets with a thickness of 4 mm using a rod of Measure the time required for dispersion into the hardness, n=5 Hardness: Measure using a Monsanto hardness tester, n=5
The measurement results are shown in Tables 2 and 3.

【表】【table】

【表】 いずれの場合も、微粉末留分を含まない崩壊剤
を使用した錠剤が優れた崩壊性を示した。
[Table] In all cases, the tablets using a disintegrant that did not contain a fine powder fraction showed excellent disintegration properties.

Claims (1)

【特許請求の範囲】[Claims] 1 無水グルコース単位当りのカルボキシメチル
基置換度が0.30〜0.80であり、145メツシユ通過
で300メツシユを通過しない粒度の繊維素グリコ
ール酸カルシウムを崩壊剤として他の賦形剤とと
もに主薬剤に添加混合して賦形することを特徴と
する崩壊性の改良された固型薬剤の製造法。
1 Calcium glycolate, which has a degree of carboxymethyl group substitution per anhydroglucose unit of 0.30 to 0.80 and has a particle size that does not pass through 145 meshes but does not pass through 300 meshes, is added to the main drug as a disintegrant and mixed with other excipients. 1. A method for producing a solid drug with improved disintegrability, characterized by forming it into a solid drug.
JP4272283A 1983-02-23 1983-03-14 Production of solid drug Granted JPS59167522A (en)

Priority Applications (2)

Application Number Priority Date Filing Date Title
JP4272283A JPS59167522A (en) 1983-03-14 1983-03-14 Production of solid drug
KR1019840000850A KR840007590A (en) 1983-02-23 1984-02-22 Method for preparing azole substituted alcohol derivative

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP4272283A JPS59167522A (en) 1983-03-14 1983-03-14 Production of solid drug

Publications (2)

Publication Number Publication Date
JPS59167522A JPS59167522A (en) 1984-09-21
JPH0532373B2 true JPH0532373B2 (en) 1993-05-14

Family

ID=12643955

Family Applications (1)

Application Number Title Priority Date Filing Date
JP4272283A Granted JPS59167522A (en) 1983-02-23 1983-03-14 Production of solid drug

Country Status (1)

Country Link
JP (1) JPS59167522A (en)

Family Cites Families (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB1560475A (en) * 1975-10-11 1980-02-06 Lilly Industries Ltd Pharmaceutical formulation
JPS59155310A (en) * 1983-02-21 1984-09-04 Daicel Chem Ind Ltd Production of solid medicinal preparation with improved disintegration

Also Published As

Publication number Publication date
JPS59167522A (en) 1984-09-21

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