JPH07277978A - Nifedipine solid particle composition for tablet production - Google Patents
Nifedipine solid particle composition for tablet productionInfo
- Publication number
- JPH07277978A JPH07277978A JP9682794A JP9682794A JPH07277978A JP H07277978 A JPH07277978 A JP H07277978A JP 9682794 A JP9682794 A JP 9682794A JP 9682794 A JP9682794 A JP 9682794A JP H07277978 A JPH07277978 A JP H07277978A
- Authority
- JP
- Japan
- Prior art keywords
- nifedipine
- tablets
- particle composition
- granulated product
- solid particle
- 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
Links
- HYIMSNHJOBLJNT-UHFFFAOYSA-N nifedipine Chemical compound COC(=O)C1=C(C)NC(C)=C(C(=O)OC)C1C1=CC=CC=C1[N+]([O-])=O HYIMSNHJOBLJNT-UHFFFAOYSA-N 0.000 title claims abstract description 73
- 229960001597 nifedipine Drugs 0.000 title claims abstract description 73
- 239000000203 mixture Substances 0.000 title claims abstract description 42
- 239000002245 particle Substances 0.000 title claims abstract description 31
- 239000007787 solid Substances 0.000 title claims abstract description 23
- 238000004519 manufacturing process Methods 0.000 title claims description 8
- 239000000244 polyoxyethylene sorbitan monooleate Substances 0.000 claims abstract description 18
- 235000010482 polyoxyethylene sorbitan monooleate Nutrition 0.000 claims abstract description 18
- 229920000053 polysorbate 80 Polymers 0.000 claims abstract description 18
- 229940068968 polysorbate 80 Drugs 0.000 claims abstract description 18
- 238000001035 drying Methods 0.000 claims abstract description 14
- 239000007864 aqueous solution Substances 0.000 claims abstract description 13
- 239000011248 coating agent Substances 0.000 claims abstract description 11
- 239000000725 suspension Substances 0.000 claims abstract description 10
- 239000000314 lubricant Substances 0.000 claims abstract description 9
- 239000007884 disintegrant Substances 0.000 claims abstract description 8
- 238000001238 wet grinding Methods 0.000 claims abstract description 6
- 239000000546 pharmaceutical excipient Substances 0.000 claims description 7
- 238000000576 coating method Methods 0.000 claims description 6
- 238000000034 method Methods 0.000 abstract description 38
- 229920002153 Hydroxypropyl cellulose Polymers 0.000 abstract description 7
- 239000001863 hydroxypropyl cellulose Substances 0.000 abstract description 7
- 235000010977 hydroxypropyl cellulose Nutrition 0.000 abstract description 7
- 238000013268 sustained release Methods 0.000 abstract description 7
- 239000012730 sustained-release form Substances 0.000 abstract description 7
- 239000000463 material Substances 0.000 abstract description 2
- 238000001704 evaporation Methods 0.000 abstract 1
- 239000003981 vehicle Substances 0.000 abstract 1
- 239000003826 tablet Substances 0.000 description 39
- 239000008187 granular material Substances 0.000 description 17
- 238000010298 pulverizing process Methods 0.000 description 17
- 238000005469 granulation Methods 0.000 description 15
- 230000003179 granulation Effects 0.000 description 15
- 239000012729 immediate-release (IR) formulation Substances 0.000 description 15
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 14
- 238000002360 preparation method Methods 0.000 description 13
- 238000007922 dissolution test Methods 0.000 description 10
- 239000003795 chemical substances by application Substances 0.000 description 9
- 239000007941 film coated tablet Substances 0.000 description 9
- 239000000243 solution Substances 0.000 description 9
- 238000009472 formulation Methods 0.000 description 7
- 239000008213 purified water Substances 0.000 description 7
- 230000002459 sustained effect Effects 0.000 description 7
- 229920002134 Carboxymethyl cellulose Polymers 0.000 description 6
- FBPFZTCFMRRESA-KVTDHHQDSA-N D-Mannitol Chemical compound OC[C@@H](O)[C@@H](O)[C@H](O)[C@H](O)CO FBPFZTCFMRRESA-KVTDHHQDSA-N 0.000 description 6
- 239000011230 binding agent Substances 0.000 description 6
- 239000001768 carboxy methyl cellulose Substances 0.000 description 6
- 235000010948 carboxy methyl cellulose Nutrition 0.000 description 6
- 239000008112 carboxymethyl-cellulose Substances 0.000 description 6
- 239000007788 liquid Substances 0.000 description 6
- HQKMJHAJHXVSDF-UHFFFAOYSA-L magnesium stearate Chemical compound [Mg+2].CCCCCCCCCCCCCCCCCC([O-])=O.CCCCCCCCCCCCCCCCCC([O-])=O HQKMJHAJHXVSDF-UHFFFAOYSA-L 0.000 description 6
- 229920003169 water-soluble polymer Polymers 0.000 description 6
- 239000002994 raw material Substances 0.000 description 5
- 239000000126 substance Substances 0.000 description 5
- 239000007939 sustained release tablet Substances 0.000 description 5
- 229920002261 Corn starch Polymers 0.000 description 4
- GWEVSGVZZGPLCZ-UHFFFAOYSA-N Titan oxide Chemical compound O=[Ti]=O GWEVSGVZZGPLCZ-UHFFFAOYSA-N 0.000 description 4
- MCMNRKCIXSYSNV-UHFFFAOYSA-N Zirconium dioxide Chemical compound O=[Zr]=O MCMNRKCIXSYSNV-UHFFFAOYSA-N 0.000 description 4
- 238000007796 conventional method Methods 0.000 description 4
- 239000008120 corn starch Substances 0.000 description 4
- 238000004090 dissolution Methods 0.000 description 4
- 239000007888 film coating Substances 0.000 description 4
- 238000009501 film coating Methods 0.000 description 4
- JEIPFZHSYJVQDO-UHFFFAOYSA-N iron(III) oxide Inorganic materials O=[Fe]O[Fe]=O JEIPFZHSYJVQDO-UHFFFAOYSA-N 0.000 description 4
- YOBAEOGBNPPUQV-UHFFFAOYSA-N iron;trihydrate Chemical compound O.O.O.[Fe].[Fe] YOBAEOGBNPPUQV-UHFFFAOYSA-N 0.000 description 4
- RMAQACBXLXPBSY-UHFFFAOYSA-N silicic acid Chemical compound O[Si](O)(O)O RMAQACBXLXPBSY-UHFFFAOYSA-N 0.000 description 4
- 235000012239 silicon dioxide Nutrition 0.000 description 4
- OGIDPMRJRNCKJF-UHFFFAOYSA-N titanium oxide Inorganic materials [Ti]=O OGIDPMRJRNCKJF-UHFFFAOYSA-N 0.000 description 4
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 description 3
- 229920002678 cellulose Polymers 0.000 description 3
- 239000001913 cellulose Substances 0.000 description 3
- 238000009826 distribution Methods 0.000 description 3
- 239000003814 drug Substances 0.000 description 3
- 230000000694 effects Effects 0.000 description 3
- 238000004108 freeze drying Methods 0.000 description 3
- 235000019359 magnesium stearate Nutrition 0.000 description 3
- 235000010355 mannitol Nutrition 0.000 description 3
- 238000004062 sedimentation Methods 0.000 description 3
- 206010002383 Angina Pectoris Diseases 0.000 description 2
- LYCAIKOWRPUZTN-UHFFFAOYSA-N Ethylene glycol Chemical compound OCCO LYCAIKOWRPUZTN-UHFFFAOYSA-N 0.000 description 2
- 206010020772 Hypertension Diseases 0.000 description 2
- 238000010521 absorption reaction Methods 0.000 description 2
- 239000000654 additive Substances 0.000 description 2
- 230000003276 anti-hypertensive effect Effects 0.000 description 2
- 229940079593 drug Drugs 0.000 description 2
- 238000010828 elution Methods 0.000 description 2
- 238000001125 extrusion Methods 0.000 description 2
- 229940031705 hydroxypropyl methylcellulose 2910 Drugs 0.000 description 2
- 238000004898 kneading Methods 0.000 description 2
- 229960003511 macrogol Drugs 0.000 description 2
- 238000002156 mixing Methods 0.000 description 2
- 230000036470 plasma concentration Effects 0.000 description 2
- 239000004014 plasticizer Substances 0.000 description 2
- 229920000136 polysorbate Polymers 0.000 description 2
- 229950008882 polysorbate Drugs 0.000 description 2
- 239000011347 resin Substances 0.000 description 2
- 229920005989 resin Polymers 0.000 description 2
- 238000003756 stirring Methods 0.000 description 2
- 238000011282 treatment Methods 0.000 description 2
- 238000005303 weighing Methods 0.000 description 2
- VBICKXHEKHSIBG-UHFFFAOYSA-N 1-monostearoylglycerol Chemical compound CCCCCCCCCCCCCCCCCC(=O)OCC(O)CO VBICKXHEKHSIBG-UHFFFAOYSA-N 0.000 description 1
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 1
- DCXXMTOCNZCJGO-UHFFFAOYSA-N Glycerol trioctadecanoate Natural products CCCCCCCCCCCCCCCCCC(=O)OCC(OC(=O)CCCCCCCCCCCCCCCCC)COC(=O)CCCCCCCCCCCCCCCCC DCXXMTOCNZCJGO-UHFFFAOYSA-N 0.000 description 1
- 206010058179 Hypertensive emergency Diseases 0.000 description 1
- FYYHWMGAXLPEAU-UHFFFAOYSA-N Magnesium Chemical compound [Mg] FYYHWMGAXLPEAU-UHFFFAOYSA-N 0.000 description 1
- 239000002202 Polyethylene glycol Substances 0.000 description 1
- 229910000831 Steel Inorganic materials 0.000 description 1
- 238000004220 aggregation Methods 0.000 description 1
- 230000002776 aggregation Effects 0.000 description 1
- 238000013019 agitation Methods 0.000 description 1
- 239000008280 blood Substances 0.000 description 1
- 210000004369 blood Anatomy 0.000 description 1
- 239000005018 casein Substances 0.000 description 1
- BECPQYXYKAMYBN-UHFFFAOYSA-N casein, tech. Chemical compound NCCCCC(C(O)=O)N=C(O)C(CC(O)=O)N=C(O)C(CCC(O)=N)N=C(O)C(CC(C)C)N=C(O)C(CCC(O)=O)N=C(O)C(CC(O)=O)N=C(O)C(CCC(O)=O)N=C(O)C(C(C)O)N=C(O)C(CCC(O)=N)N=C(O)C(CCC(O)=N)N=C(O)C(CCC(O)=N)N=C(O)C(CCC(O)=O)N=C(O)C(CCC(O)=O)N=C(O)C(COP(O)(O)=O)N=C(O)C(CCC(O)=N)N=C(O)C(N)CC1=CC=CC=C1 BECPQYXYKAMYBN-UHFFFAOYSA-N 0.000 description 1
- 235000021240 caseins Nutrition 0.000 description 1
- 230000000052 comparative effect Effects 0.000 description 1
- 239000013078 crystal Substances 0.000 description 1
- 239000003405 delayed action preparation Substances 0.000 description 1
- 230000003111 delayed effect Effects 0.000 description 1
- MCTRZKAKODSRLQ-UHFFFAOYSA-N dimethyl 2,6-dimethyl-4-(3-nitrophenyl)-1,4-dihydropyridine-3,5-dicarboxylate Chemical compound COC(=O)C1=C(C)NC(C)=C(C(=O)OC)C1C1=CC=CC([N+]([O-])=O)=C1 MCTRZKAKODSRLQ-UHFFFAOYSA-N 0.000 description 1
- 238000009505 enteric coating Methods 0.000 description 1
- 239000002702 enteric coating Substances 0.000 description 1
- 238000011049 filling Methods 0.000 description 1
- 238000005187 foaming Methods 0.000 description 1
- 210000001035 gastrointestinal tract Anatomy 0.000 description 1
- 238000000227 grinding Methods 0.000 description 1
- 230000005802 health problem Effects 0.000 description 1
- 238000001727 in vivo Methods 0.000 description 1
- 229910052749 magnesium Inorganic materials 0.000 description 1
- 239000011777 magnesium Substances 0.000 description 1
- 201000005857 malignant hypertension Diseases 0.000 description 1
- 239000000594 mannitol Substances 0.000 description 1
- 230000002085 persistent effect Effects 0.000 description 1
- 229920001223 polyethylene glycol Polymers 0.000 description 1
- 239000000843 powder Substances 0.000 description 1
- 230000002265 prevention Effects 0.000 description 1
- 229920006395 saturated elastomer Polymers 0.000 description 1
- 238000004513 sizing Methods 0.000 description 1
- 239000007901 soft capsule Substances 0.000 description 1
- 239000006104 solid solution Substances 0.000 description 1
- 239000010959 steel Substances 0.000 description 1
- 238000010998 test method Methods 0.000 description 1
- 229940126585 therapeutic drug Drugs 0.000 description 1
- 230000000304 vasodilatating effect Effects 0.000 description 1
Landscapes
- Medicinal Preparation (AREA)
- Pharmaceuticals Containing Other Organic And Inorganic Compounds (AREA)
Abstract
Description
【0001】[0001]
【産業上の利用分野】本発明は、高血圧症及び狭心症治
療用医薬として用いられるニフェジピン固体粒子組成物
に関する。更に詳しくは、本発明は、湿式粉砕により溶
解性を改善することにより、速放性及び持続性各錠剤の
いずれをも製造することが可能なニフェジピン固体粒子
組成物に関するものである。TECHNICAL FIELD The present invention relates to a nifedipine solid particle composition used as a medicine for treating hypertension and angina. More specifically, the present invention relates to a nifedipine solid particle composition capable of producing both immediate release and sustained release tablets by improving the solubility by wet milling.
【0002】[0002]
【背景技術】ニフェジピンは、優れた冠血管拡張作用を
有し、高血圧症及び狭心症発作の治療薬として広く用い
られているが、それ自体は水に難溶性の薬物であるた
め、生体利用率の高い錠剤を調製することは相当に困難
である。これまで、ニフェジピンの難溶性という水への
溶解性の問題を解決するために種々の方法が提案されて
いる。例えば、ニフェジピンをポリエチレングリコール
に溶解し、この溶液をソフトカプセルに充填する方法
(特公昭54−34048号公報参照)や、ニフェジピ
ンを固溶体として製剤化する方法(特開昭54−231
6号公報参照)がそれである。かかる方法により製造さ
れた製剤は、投与後速やかにニフェジピンの血漿中濃度
が上昇する。しかし、これらの処理により得られる製剤
は、速放性の製剤であるため、高血圧緊急症などの際の
舌下投与などには有用であるが、降圧作用の持続化は望
めないという欠点を有している。BACKGROUND ART Nifedipine has an excellent coronary vasodilatory effect and is widely used as a therapeutic drug for hypertension and angina attacks. However, since it is a drug that is poorly soluble in water, it is bioavailable. It is quite difficult to prepare high rate tablets. Until now, various methods have been proposed in order to solve the problem of the solubility of nifedipine, which is poorly soluble, in water. For example, a method of dissolving nifedipine in polyethylene glycol and filling the solution into a soft capsule (see Japanese Patent Publication No. 54-34048) or a method of formulating nifedipine as a solid solution (Japanese Patent Laid-Open No. 54-231).
This is the case (see Japanese Patent Publication No. 6). In the preparation produced by such a method, the plasma concentration of nifedipine increases immediately after administration. However, since the preparations obtained by these treatments are quick-release preparations, they are useful for sublingual administration in cases such as hypertensive emergencies, but have the drawback that a sustained antihypertensive effect cannot be expected. is doing.
【0003】また、降圧作用の持続化を得る目的で、ニ
フェジピンの放出特性を制御する方法としては、(1)
速放性製剤組成物と遅放性製剤組成物を組み合わせて持
続化をはかる方法(特開昭58−46019号公報参
照)、(2)ニフェジピンをカゼインなどと共粉砕した
後、さらに腸溶性被覆剤及び可塑剤と共粉砕したものを
乾式造粒し、持続化をはかる方法(特開昭60−255
719号公報参照)、(3)乾式粉砕により得たニフェ
ジピン結晶を用いることによって、吸収の増大及び持続
化をはかる方法(特公昭59−14446号公報参照)
などが提案されている。しかし、これらの提案された方
法は、次のような欠点を有する。(1)の方法では速放
性組成物と遅放性組成物を混合する際のバラツキがその
まま持続作用のバラツキとなる。(2)の方法では腸溶
性被覆剤を使用しているため胃腸管内容液のpHの個人
差により持続作用が影響を受ける。(3)の方法では、
粉砕後のニフェジピンの処理方法によっては好ましい持
続性が得られない場合がある。また、ニフェジピンは光
によって分解し易い薬物であるため、開放系の乾式粉砕
法では作業中の遮光性が問題となり、作業員に暗所での
作業を強いる。さらに、粉体の取り扱いは、作業性が悪
いだけでなく、作業員の健康上の問題を惹起するという
欠点を有する。Further, as a method for controlling the release characteristics of nifedipine for the purpose of obtaining a sustained antihypertensive action, the following methods are mentioned (1).
A method in which an immediate-release preparation composition and a delayed-release preparation composition are combined to achieve sustainability (see JP-A-58-46019), (2) Nifedipine is co-ground with casein, and then enteric-coated. A method in which granulation is carried out by co-grinding with a plasticizer and a plasticizer to measure the sustainability (JP-A-60-255).
719), (3) a method for increasing and maintaining absorption by using nifedipine crystals obtained by dry pulverization (see Japanese Patent Publication No. 59-14446).
Have been proposed. However, these proposed methods have the following drawbacks. In the method (1), the variation in mixing the immediate-release composition and the slow-release composition becomes the variation in the sustained action as it is. In the method (2), since the enteric coating agent is used, the sustained action is affected by the individual difference in pH of the gastrointestinal tract content liquid. In the method of (3),
Depending on the treatment method of nifedipine after pulverization, preferable sustainability may not be obtained. Further, since nifedipine is a drug that is easily decomposed by light, the light-shielding property during work is a problem in the open dry pulverization method, forcing a worker to work in a dark place. Furthermore, handling of the powder not only has poor workability, but also has the drawback of causing health problems for workers.
【0004】他方、特公昭63−112519号公報に
は、ニフェジピンを水溶性高分子物質とともに湿式粉砕
し、溶解性を改善したニフェジピン製剤が提案されてい
るが、この製剤は、使用する水の量が少ない場合は水溶
性高分子物質の濃度が高くなり、溶液の粘性が高くなる
ために製剤化しにくくなるという欠点を有している。ま
た、同公報記載の製剤は、速放性のニフェジピン製剤を
意図したものであり、持続性のニフェジピン製剤ではな
い。このように、従来の技術は、速放性製剤もしくは持
続性製剤のいずれか一方を製造する方法であり、そのど
ちらの製剤を製造するかにより、ニフェジピンの方法
は、大きく異なるものとなる。On the other hand, Japanese Patent Publication No. 63-112519 proposes a nifedipine preparation in which nifedipine is wet-milled with a water-soluble polymer substance to improve the solubility, and this preparation contains the amount of water used. When the amount is small, the concentration of the water-soluble polymer increases, and the viscosity of the solution increases, which makes it difficult to formulate the preparation. Further, the preparation described in the publication is intended as an immediate-release nifedipine preparation, and is not a sustained-release nifedipine preparation. As described above, the conventional technique is a method for producing either an immediate-release preparation or a sustained-release preparation, and the method of nifedipine varies greatly depending on which preparation is produced.
【0005】[0005]
【発明の開示】本発明者らは、ニフェジピン含有錠剤の
放出特性に影響を及ぼす要因について鋭意研究を重ねた
結果、ポリソルベート80の水溶液中において湿式粉砕
されたニフェジピンを用いることにより、速放性もしく
は持続性の錠剤を格別の製剤化技術を用いることなく任
意に製造することが可能であることを見いだした。本発
明は、かかる知見に基づいてなされたものである。DISCLOSURE OF THE INVENTION As a result of intensive studies on the factors affecting the release characteristics of tablets containing nifedipine, the present inventors have found that by using wet-ground nifedipine in an aqueous solution of polysorbate 80, rapid release or It has been found that sustained-release tablets can be made arbitrarily without the use of special formulation techniques. The present invention has been made based on such findings.
【0006】本発明は、ニフェジピンをポリソルベート
80の水溶液中において湿式粉砕し、得られた懸濁液を
乾燥して得られる錠剤製造用ニフェジピン固体粒子組成
物を提供するものである。上記ニフェジピン固体粒子組
成物を用いることにより、持続性および速放性の錠剤い
ずれをも製造することができる。The present invention provides a nifedipine solid particle composition for tablet production, which is obtained by wet milling nifedipine in an aqueous solution of polysorbate 80 and drying the resulting suspension. By using the above nifedipine solid particle composition, both sustained-release and immediate-release tablets can be produced.
【0007】持続性のニフェジピン錠を得る場合には、
ポリソルベート80の水溶液中において湿式粉砕して得
られた上記ニフェジピン固体粒子組成物に賦形剤、崩壊
剤およびヒドロキシプロピルセルロースを加えたものを
材料とし、造粒物の強度が5重量%〜20重量%になる
ように造粒を行った後、乾燥し、得られた造粒物に崩壊
剤および滑沢剤を加えて打錠を行い、得られた素錠に被
覆剤をコーティングして持続性のニフェジピン錠とす
る。他方、速放性のニフェジピン錠を得る場合には、湿
式粉砕により得られたニフェジピン固体粒子組成物に賦
形剤、崩壊剤、結合剤および滑沢剤等を加え、混合した
後、打錠を行い、得られた素錠に被覆剤をコーティング
して速放性のニフェジピン錠とする。To obtain a long-acting nifedipine tablet,
The nifedipine solid particle composition obtained by wet grinding in an aqueous solution of polysorbate 80, to which an excipient, a disintegrating agent and hydroxypropylcellulose were added, was used as a material, and the strength of the granulated product was from 5% by weight to 20% by weight. The granules are granulated so that the content of the granules becomes 100%, dried, and then the obtained granules are added with a disintegrating agent and a lubricant to form tablets, and the obtained uncoated tablets are coated with a coating agent to maintain durability. And nifedipine tablets. On the other hand, in the case of obtaining an immediate release nifedipine tablet, an excipient, a disintegrating agent, a binder, a lubricant, etc. are added to the nifedipine solid particle composition obtained by wet pulverization, and the mixture is tableted after mixing. Then, the obtained plain tablets are coated with a coating agent to give immediate release nifedipine tablets.
【0008】以下に本発明を詳細に説明する。本発明の
方法においては、まずニフェジピンがポリソルベート8
0を含む水溶液中で湿式粉砕される。ニフェジピンを乾
式粉砕あるいは水溶性高分子物質を含む水溶液中で湿式
粉砕しても、望みの放出特性を持つ錠剤を得ることはで
きない。湿式粉砕は、例えばボールミルにて行い、ポリ
ソルベート80の水溶液と共に、ニフェジピン原料を加
えて粉砕する。このとき用いるポリソルベート80はニ
フェジピンに対して4〜6重量%程度添加して行われ
る。このポリソルベート80は、湿式粉砕時にはニフェ
ジピン原料の水への分散性(凝集防止)を高め、粉砕助
剤として粉砕効率に寄与し、更に粉砕中のニフェジピン
懸濁液の泡立ちを抑えて粉砕後の取扱いを向上させる。
またポリソルベート80は、粉砕後乾燥されたニフェジ
ピン粒子の表面を覆い水への溶解性を高め、ニフェジピ
ンの生体内における吸収の改善を行っている。The present invention will be described in detail below. In the method of the present invention, first, nifedipine is polysorbate 8
It is wet-ground in an aqueous solution containing 0. Nifedipine cannot be obtained by dry pulverization or wet pulverization in an aqueous solution containing a water-soluble polymer substance to obtain tablets having desired release characteristics. The wet pulverization is performed by, for example, a ball mill, and the nifedipine raw material is added together with the aqueous solution of polysorbate 80 and pulverized. The polysorbate 80 used at this time is added by about 4 to 6% by weight with respect to nifedipine. This polysorbate 80 enhances the dispersibility (aggregation prevention) of the nifedipine raw material in water during wet pulverization, contributes to pulverization efficiency as a pulverization aid, and further suppresses the foaming of the nifedipine suspension during pulverization to handle after pulverization. Improve.
The polysorbate 80 also covers the surface of the nifedipine particles dried after pulverization to enhance the solubility in water and improve the absorption of nifedipine in vivo.
【0009】本発明における湿式粉砕は、通常ポリソル
ベート80を4〜6重量%濃度の水溶液を用いて行うの
が好ましい。ポリソルベート80の濃度をさらに高くし
て使用しても操作上何ら差し支えないが、3重量%以下
の低濃度の場合は、ニフェジピンの分散性が悪くなり好
ましくない。そして、このポリソルベート80の水溶液
をニフェジピン原料に対してほぼ等重量を用いるだけで
湿式粉砕を行うことができる。It is preferable that the wet pulverization in the present invention is generally carried out using an aqueous solution of polysorbate 80 having a concentration of 4 to 6% by weight. Even if the concentration of polysorbate 80 is further increased and used, there is no problem in the operation, but if the concentration is 3% by weight or less, the dispersibility of nifedipine is deteriorated, which is not preferable. Then, wet pulverization can be performed only by using an approximately equal weight of this aqueous solution of polysorbate 80 with respect to the nifedipine raw material.
【0010】湿式粉砕の管理は、懸濁液中のニフェジピ
ン粒子の粒径を、分散媒としてニフェジピン飽和水溶液
(メタノール:0.5重量%、ポリソルベート80:
0.05重量%を含有)を用いた沈降法により粒度分布
を測定して行われ、通常重量基準のメディアン径が10
μm以下となれば充分である。湿式粉砕されたニフェジ
ピン懸濁液は、加熱乾燥や凍結乾燥などの一般的な乾燥
方法により乾燥され、ニフェジピンは、ポリソルベート
80により被覆あるいは混合されたニフェジピン固体粒
子組成物の状態で得られる。速放性のニフェジピン錠を
目的とする場合は、加熱乾燥より、凍結乾燥による方が
適している。このようにして得られたニフェジピン固体
粒子組成物は、次の製剤化方法により、それぞれ持続性
あるいは速放性のニフェジピン錠とされる。The wet pulverization is controlled by changing the particle diameter of the nifedipine particles in the suspension to a saturated aqueous solution of nifedipine (methanol: 0.5% by weight, polysorbate 80:
(Containing 0.05% by weight) is used to measure the particle size distribution by a sedimentation method.
If it is less than μm, it is sufficient. The wet-milled nifedipine suspension is dried by a general drying method such as heat drying or freeze-drying, and nifedipine is obtained in the state of a nifedipine solid particle composition coated or mixed with polysorbate 80. For the purpose of immediate release nifedipine tablets, freeze drying is more suitable than heat drying. The nifedipine solid particle composition thus obtained is made into a sustained-release or immediate-release nifedipine tablet by the following formulation method.
【0011】(1) 持続性錠剤の製造方法 湿式粉砕後のポリソルベート80含有ニフェジピン懸濁
液を、乾燥して得られたニフェジピン固体粒子組成物に
賦形剤および崩壊剤を加えて混合し、さらに結合剤とし
て水溶性高分子物質であるヒドロキシプロピルセルロー
スの水溶液を加えて造粒する。使用する賦形剤として
は、D−マンニトール、結晶セルロース、トウモロコシ
デンプン等を、また崩壊剤としては、カルボキシメチル
セルロース等を用いることができる。(1) Method for Producing Sustained Tablets The nifedipine suspension containing polysorbate 80 after wet pulverization was mixed with an excipient and a disintegrant to the nifedipine solid particle composition obtained by drying, and further mixed. An aqueous solution of hydroxypropyl cellulose, which is a water-soluble polymer substance, is added as a binder to granulate. As the excipient to be used, D-mannitol, crystalline cellulose, corn starch and the like can be used, and as the disintegrant, carboxymethyl cellulose and the like can be used.
【0012】造粒は、練合押出造粒法、撹拌造粒法又は
流動層造粒法などの方法で行う。造粒物の乾燥は、棚式
あるいは流動層による加熱乾燥など通常の乾燥法でよ
い。乾燥後、JIS規格20メッシュの篩を通して整粒
を行う。造粒物強度15重量%以上の硬い造粒物を得る
ためには練合押出造粒法が適しており、造粒物強度が1
5重量%以下の柔らかい造粒物を得るためには流動層造
粒法が適している。また、撹拌造粒法では造粒物強度が
5重量%から30重量%の幅広い範囲の造粒物を得るこ
とができる。この際、加える水の量を多くする、または
造粒時間を長くすることにより造粒物強度の高い造粒物
が得られ、逆に水の量を少なくする、または造粒時間を
短くすることにより造粒物強度の低い造粒物が得られ
る。The granulation is performed by a method such as a kneading extrusion granulation method, a stirring granulation method or a fluidized bed granulation method. Drying of the granulated product may be carried out by an ordinary drying method such as a tray system or heat drying with a fluidized bed. After drying, the particles are sized by passing through a JIS standard 20 mesh screen. The kneading extrusion granulation method is suitable for obtaining a hard granulated product having a granulated product strength of 15% by weight or more.
The fluidized bed granulation method is suitable for obtaining a soft granulation product of 5% by weight or less. In addition, the agitation granulation method can obtain granules having a wide range of granule strength from 5% by weight to 30% by weight. At this time, by increasing the amount of water added or increasing the granulation time, a granulated product with high granule strength can be obtained, and conversely, decrease the amount of water or shorten the granulation time. As a result, a granulated product having a low granulated product strength can be obtained.
【0013】造粒物の強度の測定は、次の方法(大村
他:アビセル時報No.12(1966)p.31参
照)で行う。JIS規格20メッシュの篩を通過し、2
8メッシュの篩を通過しない造粒物20gを検体とし
て、この検体を直径0.45mm、重量0.5gのスチ
ール製ボール150個を入れた、萱垣式摩損度試験器に
投入して5分間回転し、造粒物を一部破壊せしめた後、
28メッシュの篩で篩過し、残部の全体に対する割合を
算出する。その割合を造粒物強度とする。本発明に係る
固体粒子組成物を使用した持続性ニフェジピン錠は、こ
の造粒物強度が5重量%〜20重量%の範囲で調整され
たものである。造粒物強度がこの範囲からはずれる場合
は充分な持続効果を期待できない。このように造粒物強
度の調整を行うことにより持続性が達成されることは驚
くべきことであり、ニフェジピンの持続性製剤の製造方
法における従来の技術からは全く予想できないことであ
る。The strength of the granulated product is measured by the following method (see Omura et al., Avicel Bulletin No. 12 (1966) p. 31). Passed through a JIS standard 20 mesh screen and 2
20g of granules that do not pass through an 8-mesh sieve was used as a sample, and this sample was put into a Kayagaki-type friability tester containing 150 steel balls with a diameter of 0.45mm and a weight of 0.5g and rotated for 5 minutes. After destroying some of the granules,
Sieve with a 28-mesh sieve, and calculate the ratio of the rest to the whole. The ratio is defined as the granulated product strength. The sustained-release nifedipine tablet using the solid particle composition according to the present invention has the granule strength adjusted in the range of 5% by weight to 20% by weight. If the strength of the granulated product deviates from this range, a sufficient sustaining effect cannot be expected. The fact that sustainability is achieved by adjusting the strength of the granulated product in this manner is surprising and completely unexpected from the prior art in the method for producing a sustained-release formulation of nifedipine.
【0014】次に、この造粒物に軽質無水ケイ酸あるい
はステアリン酸マグネシウムなどの滑沢剤やカルボキシ
メチルセルロースなどの崩壊剤を加え、打錠圧500〜
1,500kgで打錠を行う。崩壊剤を加えることによ
り錠剤の崩壊時間は打錠圧が変化しても大きく変動する
ことがない。次に遮光を目的とし、常法に従ってフィル
ムコーティングを行い、ニフェジピン含有持続性錠剤を
製する。コーティング剤には、人体に対する安全性が高
く、遮光効果が優れている三二酸化鉄および酸化チタン
等を遮光剤として用いることが望ましい。Next, a lubricant such as light anhydrous silicic acid or magnesium stearate and a disintegrating agent such as carboxymethyl cellulose are added to the granulated product, and the tableting pressure is 500 to 500.
Tableting is performed with 1,500 kg. By adding the disintegrant, the disintegration time of the tablet does not largely change even if the tableting pressure changes. Next, for the purpose of shielding light, film coating is performed according to a conventional method to produce a nifedipine-containing sustained-release tablet. For the coating agent, it is desirable to use iron sesquioxide, titanium oxide, or the like, which is highly safe to the human body and has an excellent light shielding effect, as a light shielding agent.
【0015】(2) 速放性錠剤の製造方法 速放性のニフェジピン錠は、湿式粉砕後のポリソルベー
ト80含有ニフェジピン懸濁液を、好ましくは凍結乾燥
により乾燥して得られたニフェジピン固体粒子組成物
に、通常錠剤に用いられる各種の添加剤を加え混練した
後常法により打錠して素錠が造られる。この場合、打錠
前に結合剤として水溶性高分子物質であるヒドロキシプ
ロピルセルロースを用いた造粒は、多くの場合持続性の
錠剤となり好ましくないが、造粒物強度が4重量%以下
程度の造粒は、水溶性高分子物質を加えて造粒しても速
放性が維持されるので差し支えない。(2) Method for Producing Immediate-Release Tablets Nifedipin tablets having immediate-release properties are obtained by drying the wet-milled polysorbate 80-containing nifedipine suspension, preferably by freeze-drying. Then, various additives usually used for tablets are added and kneaded, and then tableted by a conventional method to produce plain tablets. In this case, granulation using hydroxypropyl cellulose, which is a water-soluble polymer substance, as a binder before tableting is not preferable in many cases because it gives a sustained tablet, but granulation with a granule strength of about 4% by weight or less is preferable. The granules may be added with a water-soluble polymer substance and granulated, so that the immediate release property is maintained, which is no problem.
【0016】使用する添加剤としては、賦形剤としてD
−マンニトール、結晶セルロース、トウモロコシデンプ
ン等が、崩壊剤としてカルボキシメチルセルロース等
が、滑沢剤としては軽質無水ケイ酸、ステアリン酸マグ
ネシウム等を用いることができる。次に、得られた素錠
には、持続性錠剤の場合と同様に遮光効果が優れている
三二酸化鉄および酸化チタン等からなる遮光剤を用いて
常法に従ってコーティングされる。次に、本発明の実施
例を、対照例および各試験例と共に掲げ、本発明をさら
に詳細に説明する。本発明は、これら実施例により限定
されるものではない。The additives used are D as an excipient.
-Mannitol, crystalline cellulose, corn starch and the like, disintegrants such as carboxymethyl cellulose and the like, and lubricants such as light anhydrous silicic acid and magnesium stearate can be used. Then, the obtained plain tablets are coated by a conventional method with a light-shielding agent composed of iron sesquioxide and titanium oxide, which has an excellent light-shielding effect as in the case of the sustained-release tablet. Next, the present invention will be described in more detail with reference to Examples of the present invention together with Comparative Examples and test examples. The present invention is not limited to these examples.
【0017】[0017]
実施例1 (速放性錠剤) ニフェジピン原料200gを、ポリソルベート80 1
0gを精製水200gに溶解させた溶液に懸濁させ、内
容積が1リットルの樹脂性ボールミル用ポットに入れ、
YTZジルコニア製ボール(直径10mm)を用いて、
粉砕を行った。このときボールミルの回転速度は1分間
に100回転とした。その後、ボールミル内容物の一部
を採り沈降法による粒度分布測定を行いメディアン径が
10μm以下であることを確認した後、ボールミル内容
物を取り出し、凍結乾燥機を用いて乾燥を行い、ニフェ
ジピン固体粒子組成物195gを得た。Example 1 (immediate release tablet) 200 g of nifedipine raw material was mixed with polysorbate 801.
0 g was suspended in a solution prepared by dissolving 200 g of purified water and placed in a pot for a resin ball mill having an internal volume of 1 liter,
Using YTZ zirconia balls (diameter 10 mm),
It was crushed. At this time, the rotation speed of the ball mill was 100 rotations per minute. After that, a part of the contents of the ball mill was sampled and the particle size distribution was measured by the sedimentation method to confirm that the median diameter was 10 μm or less. Then, the contents of the ball mill were taken out and dried with a freeze dryer to obtain nifedipine solid particles. 195 g of composition was obtained.
【0018】次に、この固体粒子組成物105gに、賦
形剤としてD−マンニトール315g、トウモロコシデ
ンプン200g及び崩壊剤としてカルボキシメチルセル
ロース160gを加えて混合し、滑沢剤として軽質無水
ケイ酸10g及びステアリン酸マグネシウム10gを加
えて混合し、直径5.5mmの杵を用い、岡田精工株式
会社製単発打錠機N−30Eにて打錠圧1,000kg
で1錠80mgの素錠を得た。この素錠に下記組成のコ
ーティング液を被覆して、1錠83mgのフィルムコー
ティング錠を得た。Next, to 105 g of this solid particle composition, 315 g of D-mannitol as an excipient, 200 g of corn starch and 160 g of carboxymethyl cellulose as a disintegrant were added and mixed, and 10 g of light anhydrous silicic acid as a lubricant and stearin. 10 g of magnesium acidate was added and mixed, and using a punch having a diameter of 5.5 mm, a tableting pressure of 1,000 kg was obtained with a single-shot tableting machine N-30E manufactured by Okada Seiko Co.
Thus, 80 mg of uncoated tablets were obtained. This plain tablet was coated with a coating solution having the following composition to give a film-coated tablet (83 mg).
【0019】 コーティング液組成 ヒドロキシプロピルメチルセルロース2910 5.6部 マクロゴール6000 0.6部 酸化チタン 1.2部 三二酸化鉄 0.1部 精製水 92.5部 このフィルムコーティング錠につき、溶出試験を行った
ところ、後記溶出試験例1に示すように、この錠剤は速
放性であることが認められた。Coating liquid composition Hydroxypropyl methylcellulose 2910 5.6 parts Macrogol 6000 0.6 part Titanium oxide 1.2 parts Iron sesquioxide 0.1 part Purified water 92.5 parts Dissolution test is conducted on this film-coated tablet. As a result, as shown in the dissolution test example 1 described later, it was confirmed that the tablets had an immediate release property.
【0020】実施例2 (持続性錠剤) ニフェジピン原料2,000gを、ポリソルベート80
100gを精製水2,000gに溶解させた溶液に懸
濁させ、この懸濁液を内容積が10リットルの樹脂性ボ
ールミル用ポットに入れ、YTZジルコニア製ボール
(直径10mm)を用いて、粉砕を行った。このときボ
ールミルの回転速度は1分間に95回転とした。その
後、ボールミル内容物の一部を採り沈降法により粒度分
布測定を行いメディアン径がほぼ10μm以下であるこ
とを確認した後、ボールミル内容物を取り出し、内部温
度を約50℃にした棚式の乾燥機で15時間の乾燥を行
い、ニフェジピン固体粒子組成物1,950g得た。Example 2 (persistent tablet) 2,000 g of nifedipine raw material was added to polysorbate 80.
100 g of the product was suspended in a solution prepared by dissolving 2,000 g of purified water, the suspension was put in a pot for a resin ball mill having an internal volume of 10 liters, and pulverized using YTZ zirconia balls (diameter 10 mm). went. At this time, the rotation speed of the ball mill was 95 rotations per minute. After that, a part of the contents of the ball mill was sampled and the particle size distribution was measured by the sedimentation method to confirm that the median diameter was about 10 μm or less. Drying was carried out for 15 hours with a machine to obtain 1,950 g of a nifedipine solid particle composition.
【0021】次に、この固体粒子組成物273gに、賦
形剤としてD−マンニトール130g、結晶セルロース
390g、コーンスターチ130g及び崩壊剤としてカ
ルボキシメチルセルロース52gを加えて混合し、さら
に結合剤としてヒドロキシプロピルセルロース26gを
精製水300gに溶解させた溶液を加えて1分間撹拌造
粒を行った後、内部温度を約50℃にした棚式の乾燥機
で15時間乾燥を行い、ついで20メッシュの篩で整粒
して造粒物強度が10重量%の造粒物を得た。Next, 130 g of D-mannitol, 390 g of crystalline cellulose, 130 g of corn starch and 52 g of carboxymethyl cellulose as a disintegrating agent were added to and mixed with 273 g of the solid particle composition 263 g of hydroxypropyl cellulose as a binder. Was added to a solution of 300 g of purified water and stirred and granulated for 1 minute, followed by drying for 15 hours with a shelf-type dryer having an internal temperature of about 50 ° C., and then sizing with a 20-mesh sieve. Thus, a granulated product having a granulated product strength of 10% by weight was obtained.
【0022】次に得られた造粒物231gに、崩壊剤と
してカルボキシメチルセルロース3g、滑沢剤として軽
質無水ケイ酸3g及びステアリン酸マグネシウム3gを
加えて混合し、直径6mmの杵を用い、岡田精工株式会
社製単発打錠機N−30Eにて打錠圧1,000kgで
1錠80mgの素錠を得た。この素錠に下記組成のコー
ティング液を被覆して、1錠83mgのフィルムコーテ
ィング錠を得た。Next, 231 g of the obtained granules were mixed with 3 g of carboxymethyl cellulose as a disintegrating agent, 3 g of light anhydrous silicic acid and 3 g of magnesium stearate as a lubricant, and mixed, and using a pestle having a diameter of 6 mm, Okada Seiko Using a single-shot tableting machine N-30E manufactured by Co., Ltd., a plain tablet weighing 80 mg was obtained at a tableting pressure of 1,000 kg. This plain tablet was coated with a coating solution having the following composition to give a film-coated tablet (83 mg).
【0023】 コーティング液組成 ヒドロキシプロピルメチルセルロース2910 5.6部 マクロゴール6000 0.6部 酸化チタン 1.2部 三二酸化鉄 0.1部 精製水 92.5部Coating liquid composition Hydroxypropyl methylcellulose 2910 5.6 parts Macrogol 6000 0.6 part Titanium oxide 1.2 parts Iron sesquioxide 0.1 part Purified water 92.5 parts
【0024】このフィルムコーティング錠を健常人14
名に対して投与したところ、下記血漿中濃度試験(表
1)に示すように、ニフェジピンの最小有効血中濃度と
いわれている10ng/ml前後の血漿中濃度を12時
間にわたり安定に持続することが認められた。This film-coated tablet was used as a healthy person 14
As shown in the following plasma concentration test (Table 1), it was stably administered to plasma for about 12 ng / ml, which is said to be the minimum effective blood concentration of nifedipine, for 12 hours. Was recognized.
【0025】[0025]
【表1】 [Table 1]
【0026】実施例3 実施例2で得られたニフェジピン固体粒子組成物273
gを用い、実施例2と同様の配合処方で、結合剤として
ヒドロキシプロピルセルロース26gを精製水300m
lに溶解させた溶液を用いて30秒間撹拌造粒を行い造
粒物強度が5重量%の造粒物を得た後、この造粒物を実
施例2の方法に準じて打錠およびフィルムコーティング
を行い1錠83mgのフィルムコーティング錠を得た。Example 3 Nifedipine solid particle composition 273 obtained in Example 2
26 g of hydroxypropylcellulose as a binder in the same formulation as in Example 2, using 300 g of purified water.
After stirring and granulating for 30 seconds using the solution dissolved in 1 to obtain a granulated product having a granulated product strength of 5% by weight, the granulated product was tableted and filmed according to the method of Example 2. Coating was performed to obtain a film-coated tablet weighing 83 mg.
【0027】実施例4 実施例2で得られたニフェジピン固体粒子組成物273
gを用い、実施例2と同様の配合処方で、結合剤として
ヒドロキシプロピルセルロース26gを精製水300m
lに溶解させた溶液を用いて2分間撹拌造粒を行い造粒
物強度が20重量%の造粒物を調製した。ついでこの造
粒物について打錠およびフィルムコーティングを行い1
錠83mgのフィルムコーティング錠を得た。Example 4 Nifedipine solid particle composition 273 obtained in Example 2
26 g of hydroxypropylcellulose as a binder in the same formulation as in Example 2, using 300 g of purified water.
The solution dissolved in 1 was stirred and granulated for 2 minutes to prepare a granulated product having a granulated product strength of 20% by weight. Then, tableting and film coating of the granulated product 1
83 mg of film-coated tablets were obtained.
【0028】実施例5 実施例2で得られた造粒物強度が10重量%の造粒物を
用いて、打錠圧を500kgで1錠80mgの素錠を調
製し、この素錠に実施例2の操作法に準じてフィルムコ
ーティングを行い1錠83mgのフィルムコーティング
錠を得た。Example 5 Using the granulated product obtained in Example 2 and having a strength of 10% by weight, an uncoated tablet of 80 mg per tablet was prepared at a tableting pressure of 500 kg. Film coating was performed according to the operation method of Example 2 to obtain 83 mg of film-coated tablets.
【0029】実施例6 実施例2で得られた造粒物強度が10重量%の造粒物を
用いて、打錠圧を1,500kgで1錠80mgの素錠
を調製し、この素錠に実施例2の操作法に準じてフィル
ムコーティングを行い1錠83mgのフィルムコーティ
ング錠を得た。Example 6 Using the granulated product obtained in Example 2 and having a strength of 10% by weight, an uncoated tablet of 80 mg per tablet was prepared at a tableting pressure of 1,500 kg. Then, film coating was carried out according to the operation method of Example 2 to obtain 83 mg of film-coated tablets.
【0030】[0030]
対照例1 実施例2で得られたニフェジピン固体粒子組成物273
gを用いて、実施例2と同様の配合処方で、造粒物強度
が2重量%の造粒物を実施例2の方法に準じ打錠し、つ
いでフィルムコーティングを行って1錠83mgのフィ
ルムコーティング錠を得た。Control Example 1 Nifedipine solid particle composition 273 obtained in Example 2
Granules having the same formulation as in Example 2 but having a granule strength of 2% by weight were tableted according to the method of Example 2 and then film-coated to obtain 83 mg film. A coated tablet was obtained.
【0031】対照例2 実施例2で得られたニフェジピン固体粒子組成物273
gを用い、実施例2と同様の配合処方で、造粒物強度が
30重量%の造粒物を調製した。この造粒物について実
施例2の方法に準じて打錠を行い、ついでフィルムコー
ティングを行って1錠83mgのフィルムコーティング
錠を得た。Control Example 2 Nifedipine solid particle composition 273 obtained in Example 2
Using g, a granulated product having the same formulation as in Example 2 and a granulated product strength of 30% by weight was prepared. The granulated product was tabletted according to the method of Example 2 and then film-coated to obtain 83 mg of film-coated tablet.
【0032】〔溶出試験例1〕実施例1〜4及び対照例
1〜2の錠剤について、ニフェジピン溶出試験を溶出試
験法第2法(パドル法:日本薬局方第12局参照)に従
って行った。なお、試験液に日本薬局方第12局第1
液:無水エタノール混液(37:9)900mlを用
い、液温37℃にて行った。この溶出試験結果を表2に
示す。その結果、造粒を行わない実施例1の場合には、
15分で95%以上という速放性の溶出挙動を示し、造
粒を行った場合には、造粒物強度と溶出率の間に良好な
相関関係が示され、造粒物強度5〜20重量%の造粒物
においては、持続性錠剤として適する溶出の持続性が認
められた。[Dissolution Test Example 1] With respect to the tablets of Examples 1 to 4 and Control Examples 1 and 2, a dissolution test of nifedipine was carried out according to the dissolution test method 2 (paddle method: see Japanese Pharmacopoeia No. 12). It should be noted that the test liquid is the 12th Bureau No. 1 of the Japanese Pharmacopoeia
Liquid: A mixture of anhydrous ethanol (37: 9) (900 ml) was used and the liquid temperature was 37 ° C. The results of this dissolution test are shown in Table 2. As a result, in the case of Example 1 in which granulation is not performed,
It shows a rapid release elution behavior of 95% or more in 15 minutes, and when granulation is performed, a good correlation is shown between the granule strength and the elution rate. In the wt% granules, a sustained dissolution suitable for sustained release tablets was observed.
【0033】[0033]
【表2】 [Table 2]
【0034】〔溶出試験例2〕実施例2及び実施例5〜
6の錠剤について、溶出試験例1の方法と同一の試験法
により溶出試験を行った。その結果を表3に示す。[Dissolution Test Example 2] Example 2 and Example 5
The tablets of No. 6 were subjected to the dissolution test by the same test method as that of the dissolution test example 1. The results are shown in Table 3.
【表3】 [Table 3]
【0036】実施例2及び実施例5〜6にはニフェジピ
ンの溶出率の差はなく、打錠圧50〜1,500kgの
間で、この錠剤の溶出率は打錠圧に影響を受けないこと
が認められた。以上、溶出試験例1および2の結果から
明らかなように、ニフェジピン錠のニフェジピンの溶出
特性は、打錠圧にはほとんど影響を受けず、打錠前の造
粒物強度に依存していることが認められた。There is no difference in the dissolution rate of nifedipine between Example 2 and Examples 5-6, and the dissolution rate of the tablets was not affected by the tableting pressure when the tableting pressure was between 50 and 1,500 kg. Was recognized. As is clear from the results of the dissolution test examples 1 and 2, the dissolution characteristics of nifedipine of nifedipine tablets are hardly affected by the tableting pressure and depend on the strength of the granulated product before tableting. Admitted.
───────────────────────────────────────────────────── フロントページの続き (72)発明者 戸島 洋一 埼玉県浦和市南浦和3丁目37番地18棟204 号室 (72)発明者 榊原 大全 埼玉県久喜市青葉1丁目2番 2−504号 (72)発明者 横井 茂 東京都板橋区志村2丁目15番 24号 ─────────────────────────────────────────────────── ─── Continuation of the front page (72) Yoichi Tojima, 37, Minamiurawa, 37-chome, Urawa-shi, Saitama Prefecture, Room 18, Room No. 204 (72) Daizen Sakakibara 1-2-2-504, Aoba, Kuki-shi, Saitama Prefecture (72) ) Inventor Shigeru Yokoi 2-15-24 Shimura, Itabashi-ku, Tokyo
Claims (2)
溶液中において湿式粉砕し、得られた懸濁液を乾燥して
得られる錠剤製造用ニフェジピン固体粒子組成物。1. A nifedipine solid particle composition for tablet production, which is obtained by wet milling nifedipine in an aqueous solution of polysorbate 80, and drying the resulting suspension.
溶液中において湿式粉砕し、得られた懸濁液を乾燥して
ニフェジピン固体粒子組成物を得、この得られた固体粒
子組成物に賦形剤、崩壊剤およびヒドロキシプロピルセ
ルロースを加えたものを材料とし、造粒物の強度が5重
量%〜20重量%になるように造粒を行った後、乾燥
し、得られた造粒物に崩壊剤および滑沢剤を加えて打錠
を行い、得られた素錠に被覆剤をコーティングすること
を特徴とする持続性ニフェジピン錠の製造法。2. Nifedipine is wet-milled in an aqueous solution of polysorbate 80, the resulting suspension is dried to obtain a nifedipine solid particle composition, and an excipient and a disintegrant are added to the obtained solid particle composition. The granulated product was granulated so that the strength of the granulated product was 5% by weight to 20% by weight and then dried, and the resulting granulated product was disintegrated with a lubricant. A method for producing a long-acting nifedipine tablet, which comprises adding a lubricant to tableting, and coating the obtained plain tablet with a coating agent.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP09682794A JP3681185B2 (en) | 1994-03-31 | 1994-03-31 | Nifedipine solid particle composition for tablet production |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP09682794A JP3681185B2 (en) | 1994-03-31 | 1994-03-31 | Nifedipine solid particle composition for tablet production |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH07277978A true JPH07277978A (en) | 1995-10-24 |
| JP3681185B2 JP3681185B2 (en) | 2005-08-10 |
Family
ID=14175394
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP09682794A Expired - Fee Related JP3681185B2 (en) | 1994-03-31 | 1994-03-31 | Nifedipine solid particle composition for tablet production |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JP3681185B2 (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2001163769A (en) * | 1999-03-25 | 2001-06-19 | Otsuka Pharmaceut Co Ltd | Cilostazol preparation |
| KR100546047B1 (en) * | 2003-10-24 | 2006-01-24 | 지상철 | Sustained-release preparation of dihydropyridine-based compound and preparation method thereof |
| JP2011063611A (en) * | 1999-03-25 | 2011-03-31 | Otsuka Pharmaceut Co Ltd | Cilostazol preparation |
| JP2012046454A (en) * | 2010-08-27 | 2012-03-08 | Lion Corp | Tablet for internal use and method for producing the same |
-
1994
- 1994-03-31 JP JP09682794A patent/JP3681185B2/en not_active Expired - Fee Related
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2001163769A (en) * | 1999-03-25 | 2001-06-19 | Otsuka Pharmaceut Co Ltd | Cilostazol preparation |
| JP2011063611A (en) * | 1999-03-25 | 2011-03-31 | Otsuka Pharmaceut Co Ltd | Cilostazol preparation |
| KR100546047B1 (en) * | 2003-10-24 | 2006-01-24 | 지상철 | Sustained-release preparation of dihydropyridine-based compound and preparation method thereof |
| JP2012046454A (en) * | 2010-08-27 | 2012-03-08 | Lion Corp | Tablet for internal use and method for producing the same |
Also Published As
| Publication number | Publication date |
|---|---|
| JP3681185B2 (en) | 2005-08-10 |
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