JPS6242918A - Sustained release pharmaceutical - Google Patents

Sustained release pharmaceutical

Info

Publication number
JPS6242918A
JPS6242918A JP18091385A JP18091385A JPS6242918A JP S6242918 A JPS6242918 A JP S6242918A JP 18091385 A JP18091385 A JP 18091385A JP 18091385 A JP18091385 A JP 18091385A JP S6242918 A JPS6242918 A JP S6242918A
Authority
JP
Japan
Prior art keywords
drug
water
elution
sustained release
dissolution
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
JP18091385A
Other languages
Japanese (ja)
Inventor
Kiyoji Koyari
小鑓 喜代治
Mikio Takahashi
幹雄 高橋
Akira Ito
亮 伊藤
Masayuki Hasegawa
正行 長谷川
Shinichi Kimura
新一 木村
Takao Goto
孝夫 後藤
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.)
Kaken Pharmaceutical Co Ltd
Original Assignee
Kaken Pharmaceutical 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 Kaken Pharmaceutical Co Ltd filed Critical Kaken Pharmaceutical Co Ltd
Priority to JP18091385A priority Critical patent/JPS6242918A/en
Publication of JPS6242918A publication Critical patent/JPS6242918A/en
Pending legal-status Critical Current

Links

Abstract

PURPOSE:To economically obtain a sustained release pharmaceutical capable of surely controlling the elution of a drug without any influence of tableting pressure or hardness, by adding a water-soluble high polymer and a disintegrating agent which is another elution regulator to the drug and uniformly dispersing both components therein. CONSTITUTION:A sustained release pharmaceutical obtained by uniformly dispersing a water-soluble high polymer, e.g. hydroxypropyl methyl cellulose, polyvinylpyrrolidone (PVP) or polyvinyl alcohol (PVA), drug and a disintegrating agent, e.g. a mixture of microcrystalline cellulose with sodium carboxymethyl cellulose (CMC-Na), starch or CMC, therein and tableting the resultant mixture by a well-known method. Since a great variation in elution due to the little difference in amount of the water-soluble high polymer can be controlled by a controlling factor for accelerating the elution by the disintegrating agent which is another elution regulator, the elution of the drug can be surely controlled. Thereby, the aimed sustained release pharmaceutical can be simply and economically obtained.

Description

【発明の詳細な説明】 (産業上の利用分野) 本発明は持続性製剤に関する。[Detailed description of the invention] (Industrial application field) The present invention relates to depot formulations.

(従来の技術・発明が解決しようとする問題点)持続性
製剤、どくに持続性の1う、薬品11.投与回数を減ら
ず、寸なわち効力を持続させろ[1的、または、必要以
上に+fit +i濃度を−1−げない、すなわち副作
用を軽減する目的か1゛)種々検討がなされてきた。し
かしながら、従来より行わわでいる、いわゆるコーティ
ング法、熔融造粒法なとでは、薬物の放出特性に19い
てIコツ1−間、ロッ1へ内のバラツキが大きく、また
技術的、経済的にも満足しうるちのでばなかった。たど
えば、コーティング法については、p +−1依存性ま
たは非依存性のものがあり、■)II依存性のものは無
酸性症の患者への適用が難かしく、さらにはフィルムの
厚さく暇)を全ての顆粒または錠Δ11に均一・にしか
もピンホールなしに施すことは極めて難かしい。熔融造
粒法については、粒度分布の違いで放出量が異なったり
、錠剤の大きさ、圧力、硬度によっても放出量にかなり
影響を受けていた。叙−1−の持続性製剤の欠点を解決
するため種々の検d・1がなされており、たとえば特開
昭57−34854号、特開昭58−1・↓ 7431、 ]公報に記載の持続性製剤がある。しかし
ながら前者は、あくまで被覆jl’(合体中に17.4
ど溶出調節剤を含有する広義の:]−ティンタ法による
製剤である。そのため、被rlJ!+’(合体が溶出θ
)際に体内に残るという欠点がみl゛)れる1、まl−
後呂(911、薬物放出を水溶性高分子の添加鼠及び種
類、さらには特殊な製法により制御し、ようとした製剤
であり、水溶性高分子のみによる制御方法111、錠剤
の打錠圧、硬度により薬物の放出量が異な−)たり、特
殊製法であるため、非経済的であるとい−)欠点がみら
れる。かかる現状に鑑み、本発明t1らは、被覆重合体
を用いずに、あるいは水溶性]A″ノi分子のみによら
ず、また特殊な製造方法を必要どせずに、溶出調節剤の
水溶性高分子にさらにいまひど−)別の溶出調節剤であ
る崩壊剤を加えることにより医薬の溶出が確実に制御さ
れ、しかも通常の混合(例えば、■型混合機あるいはバ
ーチカルミキサーを用いる)操作のみで簡11jでかつ
経済的に持続性製剤を製造し・うろことを41出し、本
発明を完成するに至った。
(Problems to be solved by conventional techniques/inventions) Long-acting preparations, long-lasting drugs, drugs 11. Various studies have been conducted to maintain the efficacy without reducing the number of administrations (1) or to not increase the +fit +i concentration more than necessary, that is, to reduce side effects. However, with the so-called coating method and melt granulation method, which have been carried out in the past, there are large variations in the drug release characteristics between the two and one batch, and there is also a technical and economical problem. I was not satisfied either. For example, there are coating methods that are p+-1 dependent or independent; ■) II-dependent coating methods are difficult to apply to patients with achlorhydria, and furthermore, the thickness of the film It is extremely difficult to uniformly apply the powder to all granules or tablets Δ11 without pinholes. Regarding the melt granulation method, the amount released varies depending on the particle size distribution, and the amount released is also significantly affected by the size, pressure, and hardness of the tablet. In order to solve the shortcomings of the long-acting preparations described in Section 1-1, various tests have been carried out. There are sex preparations. However, the former is limited to covering jl' (17.4
It is a formulation prepared by the broad definition:]-Tinta method containing a dissolution regulator. Therefore, the subject rlJ! +' (coalescence is elution θ
) has the disadvantage that it remains in the body.
Goro (911) is a formulation in which drug release is controlled by the addition and type of water-soluble polymer, as well as by a special manufacturing method, control method using only water-soluble polymer 111, tablet compression pressure, Disadvantages include that the amount of drug released differs depending on the hardness, and that it is uneconomical due to the special manufacturing method. In view of the current situation, the present invention t1 et al. has developed an elution modifier that can be dissolved in water without using a coating polymer, without relying only on water-soluble A''noi molecules, and without requiring a special manufacturing method. By adding a disintegrant, which is another dissolution control agent to the polymer, the dissolution of the drug can be reliably controlled, and all that is required is a normal mixing operation (for example, using a type mixer or vertical mixer). The present invention was completed by easily and economically producing a long-lasting preparation and producing 41 scales.

(問題点を解決するだめの手段) 本発明の水溶性高分子とは、水溶性の物質で医薬の溶出
を遅らせる作用を有し、p I−1に関係なく水に溶解
する物質のことであり、さらに詳しくは、ヒドロキシプ
ロピルメチルセルロース(以下T(PMCとする)、ポ
リビニルピロリドン(以下P VPとする)、ポリビニ
ルアルコール(以下P V Aとする)、ヒドロキシプ
ロピルセルロース(以下[−1P Cとする)またはメ
チルセルロース(以トMCとする)などがあげられる。
(Means for Solving the Problem) The water-soluble polymer of the present invention is a water-soluble substance that has the effect of delaying the elution of a drug and is soluble in water regardless of p I-1. In more detail, hydroxypropyl methylcellulose (hereinafter referred to as T (PMC)), polyvinylpyrrolidone (hereinafter referred to as PVP), polyvinyl alcohol (hereinafter referred to as PVA), hydroxypropyl cellulose (hereinafter referred to as [-1PC) ) or methyl cellulose (hereinafter referred to as MC).

耐漏水溶性高分子と医薬を均一・に混合することで持続
性1 ダf!lをうることができるが、通常水溶性高分
子の少鼠添加の場合わずかな添加址の違い、操作の違い
、および錠剤もしくは顆粒の硬度により溶出率のバラツ
キが大きく再現性が乏しい。このことば、たとえば医薬
として非ピリン系消炎鎮痛剤のフルルビプロフェン(以
下FPとする)、水溶性高分子として1−T P M 
Cを用いて1例として1時間値の薬物溶出率を調べた結
果を第7表および第7図に示す。ただし、溶出試験は第
10改正日本薬局方(以下10局どする)の崩壊試験法
に準じ、溶出率ばt’ pの最大吸収波長248 nm
イ;l近にJ−9ける吸光m″から求めた。
By uniformly mixing the leakage-resistant water-soluble polymer and the medicine, the durability is 1 daf! However, when water-soluble polymers are added in small quantities, the dissolution rate varies widely due to slight differences in the addition site, differences in operation, and hardness of the tablets or granules, resulting in poor reproducibility. These words include, for example, flurbiprofen (hereinafter referred to as FP), a non-pyrine anti-inflammatory analgesic, as a medicine, and 1-TPM as a water-soluble polymer.
Table 7 and FIG. 7 show the results of examining the 1-hour drug dissolution rate using C as an example. However, the dissolution test is based on the disintegration test method of the 10th edition of the Japanese Pharmacopoeia (hereinafter referred to as 10), and the maximum absorption wavelength of t' p is 248 nm.
A: Determined from absorbance m'' in J-9 near l.

第7表 分散剤:低置換度ヒドロキシプロピル セルロース すなわち、医薬・分散剤量に対して40%(重量%、以
下同様)の水溶性高分子を用いることによ1)医薬の溶
出を制御できるようになるが40%では溶出率が53%
、30%では溶出率が80%にな−)プーリしてわずか
な水溶(’1−.高分子星の違いにより溶出のバラツキ
が大きいことが明らかである、。
Table 7 Dispersant: Low-substituted hydroxypropylcellulose, that is, 40% (wt%, same hereinafter) of water-soluble polymer based on the amount of drug/dispersant 1) By using a water-soluble polymer, the elution of the drug can be controlled. However, at 40%, the elution rate is 53%.
, at 30%, the elution rate is 80% -) There is a pulley and a slight amount of water solubility ('1-. It is clear that there is a large variation in elution due to differences in polymer stars.

そこでいまひとつ別の溶出調節剤である崩壊剤を加える
ことによりこれが溶出を速める制御因子となり医薬の溶
出を確実に制御できた。たとえば第7図に示す様に医薬
・分11Q剤に対して60%以十の水溶性高分子を用い
て多少の水溶性高分子Iの差が溶出率へ影響をry、え
ない様にした後、崩壊剤を加えることにより、錠剤及び
顆粒の硬度にほとんど影響なく、溶出率を自由に制御し
えた。つまり第7図に示す勾配の大きい直線部分でのみ
制御せずに勾配の小さい部分を利用して、その1ノベル
を崩壊剤で制御するわけである。本発明の崩壊剤とは、
医薬に用いた場合、生体に有害でないもの、たとえば微
結晶セルロースとカルボキシメチルセルロースナトリウ
ムの混合物(以下アビセルRCとする;旭化成工業株式
会社製)、デンプン、カルボキシメチルセルロース デンプン誘導体のビトロキシプロピルスターy−または
ショ糖脂肪酸エステルなどがあげ1″)れる。また、本
発明の持続性製剤は叙−■−のどとく、薬物を水溶性高
分子及び崩壊剤に均一じ混合什しめたものであるため、
医薬、たとえば抗アレルギー剤の8−へキシルオキシ−
3−(Il+−テ1ーラゾールー5ーイル)−20−ク
ロメン−2−オン(以下A L − 1 3 6とする
)(特開昭5 5−7 6 8 7 :(号公報参照)
、非ピリン系消炎鎮痛剤のフルルビプロフェン、イブプ
ロフェン、β−ブロッカ−剤の塩酸ベフノロール(特公
昭50  20063号公報参照)は10局I液中でコ
アの外周かJ≧,徐々に溶解せしめることができ、しか
も被覆重合体を用いないため通常の持続性製剤を溶出さ
せる際にみられる外皮が残る、顆粒状になった粒子が溶
出後も残るなどの欠点を有さない。
Therefore, by adding another dissolution regulator, a disintegrant, this becomes a control factor that speeds up the dissolution, and the dissolution of the drug can be reliably controlled. For example, as shown in Figure 7, by using a water-soluble polymer that accounts for 60% or more of the pharmaceutical preparation 11Q, a slight difference in water-soluble polymer I can be prevented from affecting the dissolution rate. By subsequently adding a disintegrant, the dissolution rate could be freely controlled without affecting the hardness of the tablets and granules. In other words, instead of controlling only the straight line part with a large slope shown in FIG. 7, the part with a small slope is used to control that one novel with a disintegrant. What is the disintegrant of the present invention?
When used in medicine, substances that are not harmful to living organisms, such as a mixture of microcrystalline cellulose and sodium carboxymethyl cellulose (hereinafter referred to as Avicel RC; manufactured by Asahi Kasei Corporation), starch, carboxymethyl cellulose starch derivative bitroxypropyl star y- or Sucrose fatty acid esters, etc.1'').In addition, since the long-acting preparation of the present invention uniformly mixes the drug with a water-soluble polymer and a disintegrant,
Pharmaceuticals, such as antiallergic agents 8-hexyloxy-
3-(Il+-te1-razol-5-yl)-20-chromen-2-one (hereinafter referred to as A L-136) (Japanese Patent Application Laid-open No. 5-7687: (see publication number)
Flurbiprofen, ibuprofen, a non-pyrine anti-inflammatory analgesic, and befunolol hydrochloride, a β-blocker agent (see Japanese Patent Publication No. 1983-20063), should be gradually dissolved in 10 parts I liquid to the outer periphery of the core or J≧. Furthermore, since no coating polymer is used, it does not have the disadvantages that occur when dissolving conventional long-acting preparations, such as leaving a shell or leaving granular particles even after dissolution.

本発明の持続性製剤を製造するには、医薬・分散剤量に
対して5%〜200%、好ましくは10%〜150%の
水溶性高分子と、医薬・分散剤J:マよび水溶性高分子
−眼に対して10%〜200%、−7= 好ましくは20%〜100%の崩壊剤を加え、さらに必
要に応じて賦形剤、滑沢剤を加えて均一に混合し、既知
の方法で打錠する。
To produce the long-acting preparation of the present invention, 5% to 200%, preferably 10% to 150% of the amount of the drug/dispersant is a water-soluble polymer, a drug/dispersant J: a water-soluble polymer, and a water-soluble polymer. Polymer - Add a disintegrant of 10% to 200%, -7 = preferably 20% to 100% for the eyes, and further add excipients and lubricants as necessary, mix uniformly, Compress the tablets using the following method.

また、医薬星に対し2て5%〜200%、好ましくは、
10%〜120%の水溶性高分子、または、医薬および
水溶性高分子量に対して0,1%〜200%好ましくは
1.0%〜100%の崩壊剤を加え、均一に混合し既知
の方法で製した徐放顆粒と、既知の方法で製した通常の
易溶顆粒、さらに必要に応じて滑沢剤を加えて均一に混
合し特殊な装置を用いて製剤化する多層錠あるいは有核
錠にせずに既知の方法および装置で打錠する。
In addition, 5% to 200% of the pharmaceutical star, preferably,
Add 10% to 120% of a water-soluble polymer, or 0.1% to 200%, preferably 1.0% to 100%, of a disintegrant to the pharmaceutical and water-soluble polymer weight, mix uniformly, and prepare a known Multi-layered tablets or hard-coated tablets made by adding a lubricant if necessary and mixing them uniformly using special equipment. Compress the tablets by known methods and equipment without making them into locks.

斜上のごとく本発明の製剤技術は、従来の方法となんら
変りなく、また、工程が非常に簡単であるため特別な注
意事項をもった作業標準、特別な装置なども不要であり
、簡gtな操作で、かつ経済的なものである。
As shown above, the formulation technology of the present invention is no different from conventional methods, and since the process is extremely simple, there is no need for work standards with special precautions or special equipment, and it is easy to use. It is easy to operate and economical.

一般に持続性製剤において、特に錠剤とする場合には、
いくら精度よく重景調整をしたり、打錠圧を調整しても
厚さのバラツキや硬度のバラツキが生じてくるため、溶
出歌にバラツキを生ぜしぬないようにすることは困雉で
ある。それに列して、本発明の持続性製剤は、錠剤とす
る際に打錠ハ:、硬度、大きさなどの影響がなく、工程
も捧めてt3純でありながら溶出を自在に制御すること
ができるものである。
In general, in long-acting preparations, especially in tablet form,
No matter how precisely the focus is adjusted or the tablet compression pressure is adjusted, variations in thickness and hardness will occur, so it is difficult to prevent variations in the dissolution rate. . In line with this, the long-acting preparation of the present invention has no influence on tableting, hardness, size, etc. when it is made into tablets, and it is possible to freely control dissolution while being T3-pure by dedicating the process. It is something that can be done.

(実施例) 本発明はかかる実施例のみに限定されるものではない。(Example) The present invention is not limited to such embodiments.

なお、実施例中の溶出試験は10局の崩壊試験に準じて
行い、溶出液は10局のI液もしくは■液を用いた。ま
た、溶出率は各々の薬物の最大吸収波長における吸光度
かI〕)求めた〔(株)1コ立製作所製分光光度計〕。
The elution test in the examples was carried out in accordance with the 10-station disintegration test, and the 10-station solution I or ■ solution was used as the eluent. In addition, the dissolution rate was determined by the absorbance at the maximum absorption wavelength of each drug [I]) using a spectrophotometer manufactured by Ikkotachi Seisakusho Co., Ltd.].

\、、− ゛ーーーー −“−゛−′\ 実施例1 (比較仔!D(1)(2) FT)原末            60   60 
   60低置換度ヒドロキシプロピル   25.7
  25.7   25.7セルロース(以下T、、 
I−(31どする)1(PMC9051110051,
451,451,4デンプン            
  0    27.4   54.8ステアリン酸カ
ルシウム       3    3    3上記の
成分を用いてつぎに示す方法にしたがって持続性製剤を
製造した。すなわちFP原末とL 1−T31. T−
T P M Cおよびデンプンを均一に分散させたもの
に、混合物の嵩を低くするためと流動性をよくするため
に、練合液としてイソプロピルアルコールを加え練合・
造粒し乾燥させる。さらに乾燥した顆粒にステアリン酸
カルシウムを均一に混合させたのち、7 、5 mmφ
〜8mmφの杵で打錠する。  得られた3種類の錠剤
からの薬物の溶量率を第1表および第1図に示す。
\,,- ゛ーーー−“−゛−′\ Example 1 (Comparison! D(1)(2) FT) Raw powder 60 60
60 low substituted hydroxypropyl 25.7
25.7 25.7 Cellulose (hereinafter referred to as T)
I-(31 dosuru) 1 (PMC9051110051,
451,451,4 starch
0 27.4 54.8 Calcium stearate 3 3 3 A long-acting preparation was produced using the above ingredients and according to the method shown below. That is, FP bulk powder and L 1-T31. T-
In order to reduce the bulk of the mixture and improve fluidity, isopropyl alcohol was added to the mixture of TPM C and starch that was uniformly dispersed as a kneading liquid.
Granulate and dry. Furthermore, after uniformly mixing calcium stearate with the dried granules, 7.5 mmφ
Compress into tablets with a punch of ~8 mmφ. Table 1 and FIG. 1 show the dissolution rate of the drug from the three types of tablets obtained.

第1表 第1表および第1図から明らかなように、溶出調節剤で
あるデンプンの添加により薬物の溶出率が増加すること
が判る。また溶出試験において錠剤が外周から順に徐々
に崩壊し、溶出が終了した時点では全てが完全に溶出液
に分散しているのが観察された。
As is clear from Table 1 and FIG. 1, the addition of starch as a dissolution regulator increases the dissolution rate of the drug. Further, in the dissolution test, it was observed that the tablet gradually disintegrated from the outer periphery, and by the time dissolution was completed, all the tablets were completely dispersed in the eluate.

一\、−一一一 一゛〜・へ、一 実施例2 FP原末         60    60    
60    60LT−13]、        25
.7  25.7  25.7  25.7HPMCD
O81110068,668,668,668,6CM
CI5.4  30.9  46.3  61..7ス
テアリン酸カルシウム   3   3   3   
3FP原末とLH3]、1−I P M CおよびCM
Cを均一に分散させたものに練合液としてイソプロピル
アルコールを加え練合、造粒し、乾燥させる。さらに乾
燥した顆粒にステアリン酸カルシウムを均一に混合した
のち、8mmφ〜8.5mmφの杵で打錠する。
1\, -1111゛〜・, 1 Example 2 FP bulk powder 60 60
60 60LT-13], 25
.. 7 25.7 25.7 25.7HPMCD
O81110068,668,668,668,6CM
CI5.4 30.9 46.3 61. .. 7 Calcium stearate 3 3 3
3FP bulk powder and LH3], 1-I P MC and CM
Isopropyl alcohol is added as a kneading liquid to a mixture in which C is uniformly dispersed, and the mixture is kneaded, granulated, and dried. Furthermore, after calcium stearate is uniformly mixed into the dried granules, they are compressed into tablets using a punch of 8 mm to 8.5 mm.

得られた4種類の錠剤からの薬物の溶出率を、第2表お
よび第2図に示す。
The drug dissolution rates from the four types of tablets obtained are shown in Table 2 and Figure 2.

第2表および第2図から明らかなように、溶出調節剤で
あるCMCの増量により薬物の溶出率が増えていくこと
が判る。また、溶出試験において、錠剤が外周から順に
徐々に崩壊し、溶出が終了した時点では全てが完全に溶
出液に分散しているのが観察された。
As is clear from Table 2 and FIG. 2, it can be seen that the dissolution rate of the drug increases as the amount of CMC, which is a dissolution regulator, increases. Further, in the dissolution test, it was observed that the tablet gradually disintegrated from the outer periphery, and by the time the dissolution was completed, all the tablets were completely dispersed in the eluate.

実施例3 AL−1,36原末     75   75   7
5   75Croscarmcl]ose Sodj
um   15   15   15   15HPM
C90S11100    36   45   54
   63ステアリン酸マグネシウム  9   9 
  9   9(+)    (2)     (3)
     (’I)AL−1,36原末     75
   75   75   75Croscal+ne
l 1ose 5odiu+n    15    1
5    15    15HPMC90511100
36455463アビセ/l/’RC−5915054
5861ステアリン酸マグネシウム  9   9  
 9   9上記の成分を用いて、前記実施例1と同じ
方法で製造シ、7mmφ〜8.5mmφの杵で打錠する
Example 3 AL-1,36 bulk powder 75 75 7
5 75Croscarmcl]ose Sodj
um 15 15 15 15HPM
C90S11100 36 45 54
63 Magnesium stearate 9 9
9 9(+) (2) (3)
('I) AL-1,36 original powder 75
75 75 75Croscal+ne
l 1ose 5odiu+n 15 1
5 15 15HPMC90511100
36455463 Abisse/l/'RC-5915054
5861 Magnesium stearate 9 9
9 9 Using the above ingredients, the tablets are manufactured in the same manner as in Example 1 and compressed with a punch of 7 mm to 8.5 mm.

得られた8種類の錠剤からの薬物の溶出率を、第3表お
よび第3図に示す。
Table 3 and FIG. 3 show the drug dissolution rates from the eight types of tablets obtained.

第3表 第3表および第3図から明らかなように溶出調節剤であ
るアビセルR,C−591を添加するコトにより薬物の
溶出率が増える、すなわち、溶出速度を速めることが判
った。また、溶出試験において、錠剤が外周から順に徐
々に崩壊し、溶出が終了した時点では全てが完全に溶出
液に分散しているのが観察された。
As is clear from Table 3 and FIG. 3, it was found that the addition of the dissolution regulator Avicel R, C-591 increased the dissolution rate of the drug, that is, the dissolution rate was accelerated. Further, in the dissolution test, it was observed that the tablet gradually disintegrated from the outer periphery, and by the time the dissolution was completed, all the tablets were completely dispersed in the eluate.

15一 実施例4 上記の成分を用いて、前記実施例1と同じように練合し
、穴径]、mmφのスクリーンで円筒造粒を行ない乾燥
させたものを、通常の製造方法により各顆粒を得る。
15-Example 4 The above ingredients were kneaded in the same manner as in Example 1, cylindrically granulated using a screen with a hole diameter of mmφ, and dried. get.

得られた2種類の顆粒からの薬物の溶出率を第4表およ
び第4図に示す。
Table 4 and FIG. 4 show the drug elution rates from the two types of granules obtained.

第4表 第4表および第4図から明らかなように、通常顆粒(2
)に比べ本発明による持続性顆粒(1)は、確実に薬物
の溶出率を抑制していることが判る。また、溶出試験に
おいては顆粒が徐々に崩壊し、溶出が終了した時点では
全てが完全に溶出液に分散しているのが観察された。
As is clear from Table 4 and Figure 4, normal granules (2
), it can be seen that the long-lasting granules (1) according to the present invention reliably suppress the drug dissolution rate. Furthermore, in the dissolution test, it was observed that the granules gradually disintegrated, and by the time the dissolution was completed, they were all completely dispersed in the eluate.

実施例5 易溶部(顆粒) A I、−136原末   40部 デンプン        40 徐放部(顆粒) (A) A T、 −136原未   40部 HP M C90S11 Ion    35シヨ糖脂
肪酸エステル  5 (I3) A L −1,36原未   40部 HP M C90511400035 シヨ糖脂肪酸エステル  5 −1−、記の易溶部顆粒と徐放部顆粒をそれぞれ実施例
1および実施例4の製造方法にて製造し、易溶部と徐放
部の配合比率を2:1.1:1 およびI:2に変化さ
せ、さらにその混合物にステアリン酸マグネシウA(9
mg/錠)を加え、1錠169mgの錠剤を得る。
Example 5 Easily soluble part (granules) A I, -136 bulk powder 40 parts Starch 40 Sustained release part (granules) (A) AT, -136 raw powder 40 parts HP MC C90S11 Ion 35 Sucrose fatty acid ester 5 (I3 ) A L-1,36 original 40 parts HP MC90511400035 Sucrose fatty acid ester 5-1-, the easily soluble part granules and sustained release part granules were manufactured by the manufacturing method of Example 1 and Example 4, respectively. , the blending ratio of the easily soluble part and the sustained release part was changed to 2:1.1:1 and I:2, and magnesium stearate A (9
mg/tablet) to obtain one 169 mg tablet.

得られた6種類の錠剤からの薬物の溶出率を、第5表、
第5−A図および第5−B図に示す。
Table 5 shows the dissolution rate of the drug from the six types of tablets obtained.
It is shown in FIG. 5-A and FIG. 5-B.

第5表および第5−A、B図から明らかなように易溶部
と徐放部の配合比率を変化させる、すなわち易溶部の配
合割合(吐)を高めることにより薬物の溶出率が増えて
いくことが判る。このことは通常の錠剤を製するときと
同じ方法・操作で打錠する錠剤で所期の溶出量を得るこ
とができ、特殊な装置を用いて製剤化する多層錠あるい
は有核錠にしなくてもよいことが確認された。また、溶
出試験においては錠剤が外周から順に徐々に崩壊し、溶
出が終了した時点では全てが完全に溶出液に分散してい
るのが観察された。
As is clear from Table 5 and Figures 5-A and B, by changing the blending ratio of the easily soluble part and sustained release part, that is, by increasing the blending ratio (vomit) of the easily soluble part, the dissolution rate of the drug increases. I know what's going on. This means that the desired dissolution amount can be obtained with tablets that are compressed using the same method and operation as when manufacturing regular tablets, and there is no need to use special equipment to formulate multilayer tablets or dry-coated tablets. It was confirmed that it was good. Furthermore, in the dissolution test, it was observed that the tablet gradually disintegrated from the outer periphery, and by the time dissolution was completed, all the tablets were completely dispersed in the eluate.

実施例6 易溶部(顆粒) Fp原末       30部 デンプン        30 徐放部(顆粒) (A)  FT3原末       30部HPMC9
0S11100   27 (B)  FP原末       30部HP M C
90SH400027 上記の易溶部顆粒と徐放部顆粒をそれぞれ実施例1およ
び実施例4の製造方法にて製造し、易溶部と徐放部の配
合比率、すなわち徐放部の添加率(%)を50%、60
%、70%、80%に変化させ、さらにその配合物にス
テアリン酸マグネシウム(3mg/錠)を加え、1錠1
.23mgの錠剤を得る。
Example 6 Easily soluble part (granules) Fp bulk powder 30 parts Starch 30 Sustained release part (granules) (A) FT3 bulk powder 30 parts HPMC9
0S11100 27 (B) FP bulk powder 30 copies HP MC
90SH400027 The above-mentioned easily soluble part granules and sustained release part granules were manufactured by the manufacturing method of Example 1 and Example 4, respectively, and the blending ratio of the easily soluble part and sustained release part, that is, the addition rate (%) of the sustained release part 50%, 60
%, 70%, and 80%, and further added magnesium stearate (3 mg/tablet) to the mixture, and added 1 tablet to 1 tablet.
.. Obtain 23 mg tablets.

得られた8種類の製剤の溶出率を、第6表、第6− A
図および第6−B図に示す。
The dissolution rates of the eight types of formulations obtained are shown in Table 6, Section 6-A.
and Fig. 6-B.

第6表オンよび第6−A−B図から明I)かなように徐
放部の添加敏(配合景)の増加により、薬物の溶出率が
低−トシていくことが判る。このことは通常製剤の錠剤
でも初期の溶出風を得ることができ、多層錠あるいは有
核錠にする必要がなく、実施例5と同様易溶部と徐放部
の配合比率を変化させることにより、自由に溶出皿を制
御できうろことが確認された。
As shown in Table 6 and Figures 6-A-B, it can be seen that the dissolution rate of the drug decreases as the addition sensitivity of the sustained release portion increases. This means that it is possible to obtain an initial dissolution effect even with tablets of ordinary formulations, and there is no need to make them into multilayer tablets or hard-coated tablets. It was confirmed that the elution dish could be freely controlled.

(発明の効果) 以上述べたごとく本発明の持続性製剤は、従来のような
被覆重合体を用いた製剤や特殊な製造方法を必要とする
製剤と異なり、溶出調節剤の水溶性高分子にさらにいま
ひとつ別の溶出調節剤である崩壊剤を加えることにより
、打錠圧や硬度(錠剤の場合)に影響を受けずに医薬の
溶出基のバラツキを少なく制御しうろことができるもの
である。
(Effects of the Invention) As described above, the long-acting formulation of the present invention differs from conventional formulations using coated polymers or formulations requiring special manufacturing methods, in that the long-acting formulation of the present invention does not require a water-soluble polymer as a dissolution regulator. Furthermore, by adding a disintegrant, which is another dissolution control agent, it is possible to control the dispersion of the dissolution group of the drug to a minimum without being affected by tableting pressure or hardness (in the case of tablets).

また、通常の混合をするという操作のみで簡単でかつ経
済的に持続性製剤を製造しうろことができる。
In addition, long-lasting preparations can be produced simply and economically by just the usual mixing operation.

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

第1〜6A図j3よび6−B図はそれぞれ実施例1〜6
でえられた持続性製剤の溶出試験の結果を示すグラフ、
第7図は水溶性高分子量と溶出率の関係を示すグラフで
ある。
Figures 1 to 6A j3 and Figures 6-B are Examples 1 to 6, respectively.
A graph showing the results of a dissolution test of the obtained long-acting formulation,
FIG. 7 is a graph showing the relationship between water-soluble polymer weight and elution rate.

Claims (1)

【特許請求の範囲】 1 水溶性高分子と医薬および崩壊剤が均一に分散され
てなることを特徴とする持続性製剤。 2 水溶性高分子がヒドロキシプロピルメチルセルロー
ス、ポリビニルピロリドン、ポリビニルアルコール、ヒ
ドロキシプロピルセルロース、またはメチルセルロース
である特許請求の範囲第1項記載の持続性製剤。 3 崩壊剤が微結晶セルロースとカルボキシメチルセル
ロースナトリウムの混合物、デンプン、カルボキシメチ
ルセルロース、デンプン誘導体のヒドロキシプロピルス
ターチまたはショ糖脂肪酸エステルである特許請求の範
囲第1項または第2項記載の持続性製剤。 4 水溶性高分子と医薬および崩壊剤が均一に分散され
てなる徐放部および通常の医薬で構成された易溶部とか
らなる特許請求の範囲第1項記載の持続性製剤。 5 水溶性高分子がヒドロキシプロピルメチルセルロー
ス、ポリビニルピロリドン、ポリビニルアルコール、ヒ
ドロキシプロピルセルロースまたはメチルセルロースで
ある特許請求の範囲第4項記載の持続性製剤。 6 崩壊剤が微結晶セルロースとカルボキシメチルセル
ロースナトリウムの混合物、デンプン、カルボキシメチ
ルセルロース、デンプン誘導体のヒドロキシプロピルス
ターチ、またはショ糖脂肪酸エステルである特許請求の
範囲第4項または第5項記載の持続性製剤。
[Scope of Claims] 1. A long-lasting preparation characterized by uniformly dispersing a water-soluble polymer, a drug, and a disintegrant. 2. The long-acting preparation according to claim 1, wherein the water-soluble polymer is hydroxypropylmethylcellulose, polyvinylpyrrolidone, polyvinyl alcohol, hydroxypropylcellulose, or methylcellulose. 3. The sustained-release preparation according to claim 1 or 2, wherein the disintegrant is a mixture of microcrystalline cellulose and sodium carboxymethyl cellulose, starch, carboxymethyl cellulose, hydroxypropyl starch of a starch derivative, or sucrose fatty acid ester. 4. The long-acting preparation according to claim 1, comprising a sustained release part in which a water-soluble polymer, a drug, and a disintegrant are uniformly dispersed, and an easily soluble part made of a conventional drug. 5. The long-acting preparation according to claim 4, wherein the water-soluble polymer is hydroxypropylmethylcellulose, polyvinylpyrrolidone, polyvinyl alcohol, hydroxypropylcellulose, or methylcellulose. 6. The sustained-release preparation according to claim 4 or 5, wherein the disintegrant is a mixture of microcrystalline cellulose and sodium carboxymethyl cellulose, starch, carboxymethyl cellulose, hydroxypropyl starch, a starch derivative, or sucrose fatty acid ester.
JP18091385A 1985-08-20 1985-08-20 Sustained release pharmaceutical Pending JPS6242918A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP18091385A JPS6242918A (en) 1985-08-20 1985-08-20 Sustained release pharmaceutical

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP18091385A JPS6242918A (en) 1985-08-20 1985-08-20 Sustained release pharmaceutical

Publications (1)

Publication Number Publication Date
JPS6242918A true JPS6242918A (en) 1987-02-24

Family

ID=16091477

Family Applications (1)

Application Number Title Priority Date Filing Date
JP18091385A Pending JPS6242918A (en) 1985-08-20 1985-08-20 Sustained release pharmaceutical

Country Status (1)

Country Link
JP (1) JPS6242918A (en)

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2008526879A (en) * 2005-01-06 2008-07-24 シーブイ・セラピューティクス・インコーポレイテッド Sustained release pharmaceutical formulation containing ranolazine
JP2009538912A (en) * 2006-05-31 2009-11-12 バーテックス ファーマシューティカルズ インコーポレイテッド Oral controlled release dosage form of interleukin-1β converting enzyme inhibitor
US8114883B2 (en) 2007-12-04 2012-02-14 Landec Corporation Polymer formulations for delivery of bioactive materials
US8399007B2 (en) 2006-12-05 2013-03-19 Landec Corporation Method for formulating a controlled-release pharmaceutical formulation
US8956602B2 (en) 2006-12-05 2015-02-17 Landec, Inc. Delivery of drugs

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2008526879A (en) * 2005-01-06 2008-07-24 シーブイ・セラピューティクス・インコーポレイテッド Sustained release pharmaceutical formulation containing ranolazine
JP2009538912A (en) * 2006-05-31 2009-11-12 バーテックス ファーマシューティカルズ インコーポレイテッド Oral controlled release dosage form of interleukin-1β converting enzyme inhibitor
US8399007B2 (en) 2006-12-05 2013-03-19 Landec Corporation Method for formulating a controlled-release pharmaceutical formulation
US8956602B2 (en) 2006-12-05 2015-02-17 Landec, Inc. Delivery of drugs
US8114883B2 (en) 2007-12-04 2012-02-14 Landec Corporation Polymer formulations for delivery of bioactive materials

Similar Documents

Publication Publication Date Title
CA1315202C (en) Oral sustained release acetaminophen formulation and process
KR100463496B1 (en) Sustained release matrix systems for highly soluble drugs
JP2638389B2 (en) Sustained-release matrix tablets of indapamide after oral administration
WO2006094083A1 (en) Controlled release venlafaxine formulations
EP0221732A2 (en) Sustained release tablets
WO1999053905A1 (en) Multiple-unit sustained release tablets
US20030099710A1 (en) Granule modulating hydrogel system
MXPA04009701A (en) Sustained release metoprolol formulations.
KR20060103330A (en) Sustained release torsemide dosage forms
JPS6242918A (en) Sustained release pharmaceutical
JP2022544167A (en) Pharmaceutical composition containing nitroxoline, nitroxoline oral solid tablet, method of preparation thereof, and use thereof
JP6328138B2 (en) Of N- [5- [2- (3,5-dimethoxyphenyl) ethyl] -2H-pyrazol-3-yl] -4-[(3R, 5S) -3,5-dimethylpiperazin-1-yl] benzamide Pharmaceutical formulation
CN113288905A (en) Pharmaceutical composition containing dortavir sodium, lamivudine and norfovir disoproxil fumarate
KR101175816B1 (en) Sustained release tablet for oral use
CN113368073A (en) Method for producing a pharmaceutical preparation for reducing blood uric acid levels
JPH11180875A (en) Theophylline sustained release tablet and its production
JP2020180101A (en) Method for Producing Levetiracetam-Containing Pharmaceutical Composition
WO2024024865A1 (en) Levodopa sustained release formulation
CN109568281B (en) Sulfasalazine tablet and preparation method thereof
WO2022042646A1 (en) Lurasidone hydrochloride composition and preparation method therefor
JP2017075138A (en) Dienogest-containing tablet
CN110719782B (en) Pharmaceutical composition containing third-generation small molecule EGFR inhibitor and preparation method thereof
JPH02282323A (en) Production of sustained release tablet
JP6002869B1 (en) Dienogest-containing tablets
JPH115739A (en) Prolonged action drug containing bezafibrate and manufacture of the same