JPS6137247B2 - - Google Patents
Info
- Publication number
- JPS6137247B2 JPS6137247B2 JP15433077A JP15433077A JPS6137247B2 JP S6137247 B2 JPS6137247 B2 JP S6137247B2 JP 15433077 A JP15433077 A JP 15433077A JP 15433077 A JP15433077 A JP 15433077A JP S6137247 B2 JPS6137247 B2 JP S6137247B2
- Authority
- JP
- Japan
- Prior art keywords
- cyclodextrin
- glucan
- tablets
- mixed
- tablet
- 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
Links
- 229920000858 Cyclodextrin Polymers 0.000 claims description 46
- 239000000203 mixture Substances 0.000 claims description 46
- 239000001116 FEMA 4028 Substances 0.000 claims description 39
- WHGYBXFWUBPSRW-FOUAGVGXSA-N beta-cyclodextrin Chemical compound OC[C@H]([C@H]([C@@H]([C@H]1O)O)O[C@H]2O[C@@H]([C@@H](O[C@H]3O[C@H](CO)[C@H]([C@@H]([C@H]3O)O)O[C@H]3O[C@H](CO)[C@H]([C@@H]([C@H]3O)O)O[C@H]3O[C@H](CO)[C@H]([C@@H]([C@H]3O)O)O[C@H]3O[C@H](CO)[C@H]([C@@H]([C@H]3O)O)O3)[C@H](O)[C@H]2O)CO)O[C@@H]1O[C@H]1[C@H](O)[C@@H](O)[C@@H]3O[C@@H]1CO WHGYBXFWUBPSRW-FOUAGVGXSA-N 0.000 claims description 39
- 235000011175 beta-cyclodextrine Nutrition 0.000 claims description 39
- 229960004853 betadex Drugs 0.000 claims description 39
- 239000004615 ingredient Substances 0.000 claims description 38
- 229920001503 Glucan Polymers 0.000 claims description 24
- 239000000546 pharmaceutical excipient Substances 0.000 claims description 21
- 239000007787 solid Substances 0.000 claims description 14
- 238000002360 preparation method Methods 0.000 claims description 13
- 238000002441 X-ray diffraction Methods 0.000 claims description 11
- 239000008194 pharmaceutical composition Substances 0.000 claims description 5
- 239000000126 substance Substances 0.000 claims description 5
- HFHDHCJBZVLPGP-UHFFFAOYSA-N schardinger α-dextrin Chemical compound O1C(C(C2O)O)C(CO)OC2OC(C(C2O)O)C(CO)OC2OC(C(C2O)O)C(CO)OC2OC(C(O)C2O)C(CO)OC2OC(C(C2O)O)C(CO)OC2OC2C(O)C(O)C1OC2CO HFHDHCJBZVLPGP-UHFFFAOYSA-N 0.000 claims description 4
- 239000003826 tablet Substances 0.000 description 53
- 238000002156 mixing Methods 0.000 description 23
- 238000000034 method Methods 0.000 description 21
- HQKMJHAJHXVSDF-UHFFFAOYSA-L magnesium stearate Chemical compound [Mg+2].CCCCCCCCCCCCCCCCCC([O-])=O.CCCCCCCCCCCCCCCCCC([O-])=O HQKMJHAJHXVSDF-UHFFFAOYSA-L 0.000 description 20
- 239000008187 granular material Substances 0.000 description 17
- 239000001913 cellulose Substances 0.000 description 16
- 238000004090 dissolution Methods 0.000 description 16
- 229920002678 cellulose Polymers 0.000 description 15
- 239000000843 powder Substances 0.000 description 15
- 239000002775 capsule Substances 0.000 description 14
- 238000009472 formulation Methods 0.000 description 14
- 238000010298 pulverizing process Methods 0.000 description 14
- 238000000227 grinding Methods 0.000 description 11
- 239000000654 additive Substances 0.000 description 10
- 239000000314 lubricant Substances 0.000 description 10
- 235000019359 magnesium stearate Nutrition 0.000 description 10
- GUBGYTABKSRVRQ-QKKXKWKRSA-N Lactose Natural products OC[C@H]1O[C@@H](O[C@H]2[C@H](O)[C@@H](O)C(O)O[C@@H]2CO)[C@H](O)[C@@H](O)[C@H]1O GUBGYTABKSRVRQ-QKKXKWKRSA-N 0.000 description 9
- 239000011230 binding agent Substances 0.000 description 9
- 239000003795 chemical substances by application Substances 0.000 description 9
- 239000008101 lactose Substances 0.000 description 9
- 238000007907 direct compression Methods 0.000 description 8
- 238000004519 manufacturing process Methods 0.000 description 8
- 230000000694 effects Effects 0.000 description 7
- 238000005259 measurement Methods 0.000 description 7
- 239000000047 product Substances 0.000 description 7
- CPJSUEIXXCENMM-UHFFFAOYSA-N phenacetin Chemical compound CCOC1=CC=C(NC(C)=O)C=C1 CPJSUEIXXCENMM-UHFFFAOYSA-N 0.000 description 6
- 229920002472 Starch Polymers 0.000 description 5
- NHUHCSRWZMLRLA-UHFFFAOYSA-N Sulfisoxazole Chemical compound CC1=NOC(NS(=O)(=O)C=2C=CC(N)=CC=2)=C1C NHUHCSRWZMLRLA-UHFFFAOYSA-N 0.000 description 5
- 238000007906 compression Methods 0.000 description 5
- 230000006835 compression Effects 0.000 description 5
- 238000010828 elution Methods 0.000 description 5
- 238000011049 filling Methods 0.000 description 5
- 239000008107 starch Substances 0.000 description 5
- 235000019698 starch Nutrition 0.000 description 5
- 229960000654 sulfafurazole Drugs 0.000 description 5
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 5
- 230000000996 additive effect Effects 0.000 description 4
- 239000000796 flavoring agent Substances 0.000 description 4
- 235000013355 food flavoring agent Nutrition 0.000 description 4
- -1 mannitrate Substances 0.000 description 4
- 238000000465 moulding Methods 0.000 description 4
- 238000004806 packaging method and process Methods 0.000 description 4
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 3
- WIIZWVCIJKGZOK-RKDXNWHRSA-N chloramphenicol Chemical compound ClC(Cl)C(=O)N[C@H](CO)[C@H](O)C1=CC=C([N+]([O-])=O)C=C1 WIIZWVCIJKGZOK-RKDXNWHRSA-N 0.000 description 3
- 229960005091 chloramphenicol Drugs 0.000 description 3
- 239000003086 colorant Substances 0.000 description 3
- 230000006866 deterioration Effects 0.000 description 3
- 238000005469 granulation Methods 0.000 description 3
- 230000003179 granulation Effects 0.000 description 3
- 229960003893 phenacetin Drugs 0.000 description 3
- 230000000704 physical effect Effects 0.000 description 3
- 229920003023 plastic Polymers 0.000 description 3
- 239000004033 plastic Substances 0.000 description 3
- 229920002134 Carboxymethyl cellulose Polymers 0.000 description 2
- ULGZDMOVFRHVEP-RWJQBGPGSA-N Erythromycin Chemical compound O([C@@H]1[C@@H](C)C(=O)O[C@@H]([C@@]([C@H](O)[C@@H](C)C(=O)[C@H](C)C[C@@](C)(O)[C@H](O[C@H]2[C@@H]([C@H](C[C@@H](C)O2)N(C)C)O)[C@H]1C)(C)O)CC)[C@H]1C[C@@](C)(OC)[C@@H](O)[C@H](C)O1 ULGZDMOVFRHVEP-RWJQBGPGSA-N 0.000 description 2
- 229920002153 Hydroxypropyl cellulose Polymers 0.000 description 2
- 238000010521 absorption reaction Methods 0.000 description 2
- 238000003677 abuse test Methods 0.000 description 2
- 230000008901 benefit Effects 0.000 description 2
- RYYVLZVUVIJVGH-UHFFFAOYSA-N caffeine Chemical compound CN1C(=O)N(C)C(=O)C2=C1N=CN2C RYYVLZVUVIJVGH-UHFFFAOYSA-N 0.000 description 2
- OSGAYBCDTDRGGQ-UHFFFAOYSA-L calcium sulfate Chemical compound [Ca+2].[O-]S([O-])(=O)=O OSGAYBCDTDRGGQ-UHFFFAOYSA-L 0.000 description 2
- 239000001768 carboxy methyl cellulose Substances 0.000 description 2
- 235000010948 carboxy methyl cellulose Nutrition 0.000 description 2
- 239000008112 carboxymethyl-cellulose Substances 0.000 description 2
- 229940105329 carboxymethylcellulose Drugs 0.000 description 2
- 230000008859 change Effects 0.000 description 2
- 239000007891 compressed tablet Substances 0.000 description 2
- 238000000748 compression moulding Methods 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 239000007884 disintegrant Substances 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 238000011156 evaluation Methods 0.000 description 2
- 239000001863 hydroxypropyl cellulose Substances 0.000 description 2
- 235000010977 hydroxypropyl cellulose Nutrition 0.000 description 2
- 239000001866 hydroxypropyl methyl cellulose Substances 0.000 description 2
- 235000010979 hydroxypropyl methyl cellulose Nutrition 0.000 description 2
- 229920003088 hydroxypropyl methyl cellulose Polymers 0.000 description 2
- 239000007788 liquid Substances 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 229920000609 methyl cellulose Polymers 0.000 description 2
- 239000001923 methylcellulose Substances 0.000 description 2
- 235000010981 methylcellulose Nutrition 0.000 description 2
- GLDOVTGHNKAZLK-UHFFFAOYSA-N octadecan-1-ol Chemical compound CCCCCCCCCCCCCCCCCCO GLDOVTGHNKAZLK-UHFFFAOYSA-N 0.000 description 2
- 239000002994 raw material Substances 0.000 description 2
- 239000002904 solvent Substances 0.000 description 2
- 229910001220 stainless steel Inorganic materials 0.000 description 2
- 239000010935 stainless steel Substances 0.000 description 2
- 239000000454 talc Substances 0.000 description 2
- 229910052623 talc Inorganic materials 0.000 description 2
- ZFXYFBGIUFBOJW-UHFFFAOYSA-N theophylline Chemical compound O=C1N(C)C(=O)N(C)C2=C1NC=N2 ZFXYFBGIUFBOJW-UHFFFAOYSA-N 0.000 description 2
- 238000005303 weighing Methods 0.000 description 2
- DSSYKIVIOFKYAU-XCBNKYQSSA-N (R)-camphor Chemical compound C1C[C@@]2(C)C(=O)C[C@@H]1C2(C)C DSSYKIVIOFKYAU-XCBNKYQSSA-N 0.000 description 1
- GCKMFJBGXUYNAG-UHFFFAOYSA-N 17alpha-methyltestosterone Natural products C1CC2=CC(=O)CCC2(C)C2C1C1CCC(C)(O)C1(C)CC2 GCKMFJBGXUYNAG-UHFFFAOYSA-N 0.000 description 1
- ZRPAUEVGEGEPFQ-UHFFFAOYSA-N 2-[4-[2-(2,3-dihydro-1H-inden-2-ylamino)pyrimidin-5-yl]pyrazol-1-yl]-1-(2,4,6,7-tetrahydrotriazolo[4,5-c]pyridin-5-yl)ethanone Chemical compound C1C(CC2=CC=CC=C12)NC1=NC=C(C=N1)C=1C=NN(C=1)CC(=O)N1CC2=C(CC1)NN=N2 ZRPAUEVGEGEPFQ-UHFFFAOYSA-N 0.000 description 1
- 229920001450 Alpha-Cyclodextrin Polymers 0.000 description 1
- GUBGYTABKSRVRQ-XLOQQCSPSA-N Alpha-Lactose Chemical compound O[C@@H]1[C@@H](O)[C@@H](O)[C@@H](CO)O[C@H]1O[C@@H]1[C@@H](CO)O[C@H](O)[C@H](O)[C@H]1O GUBGYTABKSRVRQ-XLOQQCSPSA-N 0.000 description 1
- OYPRJOBELJOOCE-UHFFFAOYSA-N Calcium Chemical compound [Ca] OYPRJOBELJOOCE-UHFFFAOYSA-N 0.000 description 1
- 241000723346 Cinnamomum camphora Species 0.000 description 1
- 229920001353 Dextrin Polymers 0.000 description 1
- 239000004375 Dextrin Substances 0.000 description 1
- WQZGKKKJIJFFOK-GASJEMHNSA-N Glucose Natural products OC[C@H]1OC(O)[C@H](O)[C@@H](O)[C@@H]1O WQZGKKKJIJFFOK-GASJEMHNSA-N 0.000 description 1
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 1
- LPHGQDQBBGAPDZ-UHFFFAOYSA-N Isocaffeine Natural products CN1C(=O)N(C)C(=O)C2=C1N(C)C=N2 LPHGQDQBBGAPDZ-UHFFFAOYSA-N 0.000 description 1
- 241000758791 Juglandaceae Species 0.000 description 1
- GCKMFJBGXUYNAG-HLXURNFRSA-N Methyltestosterone Chemical compound C1CC2=CC(=O)CC[C@]2(C)[C@@H]2[C@@H]1[C@@H]1CC[C@](C)(O)[C@@]1(C)CC2 GCKMFJBGXUYNAG-HLXURNFRSA-N 0.000 description 1
- 229920000881 Modified starch Polymers 0.000 description 1
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 1
- CZMRCDWAGMRECN-UGDNZRGBSA-N Sucrose Chemical compound O[C@H]1[C@H](O)[C@@H](CO)O[C@@]1(CO)O[C@@H]1[C@H](O)[C@@H](O)[C@H](O)[C@@H](CO)O1 CZMRCDWAGMRECN-UGDNZRGBSA-N 0.000 description 1
- 229930006000 Sucrose Natural products 0.000 description 1
- 235000010724 Wisteria floribunda Nutrition 0.000 description 1
- 238000002835 absorbance Methods 0.000 description 1
- 238000005903 acid hydrolysis reaction Methods 0.000 description 1
- 239000004480 active ingredient Substances 0.000 description 1
- 239000003513 alkali Substances 0.000 description 1
- 230000004075 alteration Effects 0.000 description 1
- CEGOLXSVJUTHNZ-UHFFFAOYSA-K aluminium tristearate Chemical compound [Al+3].CCCCCCCCCCCCCCCCCC([O-])=O.CCCCCCCCCCCCCCCCCC([O-])=O.CCCCCCCCCCCCCCCCCC([O-])=O CEGOLXSVJUTHNZ-UHFFFAOYSA-K 0.000 description 1
- 229940063655 aluminum stearate Drugs 0.000 description 1
- 229960000723 ampicillin Drugs 0.000 description 1
- AVKUERGKIZMTKX-NJBDSQKTSA-N ampicillin Chemical compound C1([C@@H](N)C(=O)N[C@H]2[C@H]3SC([C@@H](N3C2=O)C(O)=O)(C)C)=CC=CC=C1 AVKUERGKIZMTKX-NJBDSQKTSA-N 0.000 description 1
- 230000003115 biocidal effect Effects 0.000 description 1
- 229960001948 caffeine Drugs 0.000 description 1
- VJEONQKOZGKCAK-UHFFFAOYSA-N caffeine Natural products CN1C(=O)N(C)C(=O)C2=C1C=CN2C VJEONQKOZGKCAK-UHFFFAOYSA-N 0.000 description 1
- 239000011575 calcium Substances 0.000 description 1
- 229910052791 calcium Inorganic materials 0.000 description 1
- 239000001506 calcium phosphate Substances 0.000 description 1
- 229910000389 calcium phosphate Inorganic materials 0.000 description 1
- 235000011010 calcium phosphates Nutrition 0.000 description 1
- 159000000007 calcium salts Chemical class 0.000 description 1
- CJZGTCYPCWQAJB-UHFFFAOYSA-L calcium stearate Chemical compound [Ca+2].CCCCCCCCCCCCCCCCCC([O-])=O.CCCCCCCCCCCCCCCCCC([O-])=O CJZGTCYPCWQAJB-UHFFFAOYSA-L 0.000 description 1
- 239000008116 calcium stearate Substances 0.000 description 1
- 235000013539 calcium stearate Nutrition 0.000 description 1
- 238000011088 calibration curve Methods 0.000 description 1
- 229960000846 camphor Drugs 0.000 description 1
- 229930008380 camphor Natural products 0.000 description 1
- 239000007963 capsule composition Substances 0.000 description 1
- 229940084030 carboxymethylcellulose calcium Drugs 0.000 description 1
- 229920006184 cellulose methylcellulose Polymers 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 239000000470 constituent Substances 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 235000019425 dextrin Nutrition 0.000 description 1
- WQABCVAJNWAXTE-UHFFFAOYSA-N dimercaprol Chemical compound OCC(S)CS WQABCVAJNWAXTE-UHFFFAOYSA-N 0.000 description 1
- 229960001051 dimercaprol Drugs 0.000 description 1
- 230000008034 disappearance Effects 0.000 description 1
- 239000012738 dissolution medium Substances 0.000 description 1
- 239000002552 dosage form Substances 0.000 description 1
- 229940079593 drug Drugs 0.000 description 1
- 239000003814 drug Substances 0.000 description 1
- 238000005538 encapsulation Methods 0.000 description 1
- 229960003276 erythromycin Drugs 0.000 description 1
- 238000002474 experimental method Methods 0.000 description 1
- 230000002349 favourable effect Effects 0.000 description 1
- 239000000945 filler Substances 0.000 description 1
- 239000012467 final product Substances 0.000 description 1
- 239000004503 fine granule Substances 0.000 description 1
- 239000010419 fine particle Substances 0.000 description 1
- 235000013305 food Nutrition 0.000 description 1
- 239000008103 glucose Substances 0.000 description 1
- UFVKGYZPFZQRLF-UHFFFAOYSA-N hydroxypropyl methyl cellulose Chemical compound OC1C(O)C(OC)OC(CO)C1OC1C(O)C(O)C(OC2C(C(O)C(OC3C(C(O)C(O)C(CO)O3)O)C(CO)O2)O)C(CO)O1 UFVKGYZPFZQRLF-UHFFFAOYSA-N 0.000 description 1
- 230000006872 improvement Effects 0.000 description 1
- 238000001727 in vivo Methods 0.000 description 1
- 239000003456 ion exchange resin Substances 0.000 description 1
- 229920003303 ion-exchange polymer Polymers 0.000 description 1
- 239000000395 magnesium oxide Substances 0.000 description 1
- CPLXHLVBOLITMK-UHFFFAOYSA-N magnesium oxide Inorganic materials [Mg]=O CPLXHLVBOLITMK-UHFFFAOYSA-N 0.000 description 1
- AXZKOIWUVFPNLO-UHFFFAOYSA-N magnesium;oxygen(2-) Chemical compound [O-2].[Mg+2] AXZKOIWUVFPNLO-UHFFFAOYSA-N 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 229960001566 methyltestosterone Drugs 0.000 description 1
- 239000011812 mixed powder Substances 0.000 description 1
- 235000019426 modified starch Nutrition 0.000 description 1
- GOQYKNQRPGWPLP-UHFFFAOYSA-N n-heptadecyl alcohol Natural products CCCCCCCCCCCCCCCCCO GOQYKNQRPGWPLP-UHFFFAOYSA-N 0.000 description 1
- QIQXTHQIDYTFRH-UHFFFAOYSA-N octadecanoic acid Chemical compound CCCCCCCCCCCCCCCCCC(O)=O QIQXTHQIDYTFRH-UHFFFAOYSA-N 0.000 description 1
- 229920001542 oligosaccharide Polymers 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 239000001267 polyvinylpyrrolidone Substances 0.000 description 1
- 229920000036 polyvinylpyrrolidone Polymers 0.000 description 1
- 235000013855 polyvinylpyrrolidone Nutrition 0.000 description 1
- 229910052573 porcelain Inorganic materials 0.000 description 1
- 239000011148 porous material Substances 0.000 description 1
- 230000008569 process Effects 0.000 description 1
- 238000004904 shortening Methods 0.000 description 1
- 229910052814 silicon oxide Inorganic materials 0.000 description 1
- 159000000000 sodium salts Chemical class 0.000 description 1
- 239000005720 sucrose Substances 0.000 description 1
- 230000002195 synergetic effect Effects 0.000 description 1
- 238000012360 testing method Methods 0.000 description 1
- 229960000278 theophylline Drugs 0.000 description 1
- 238000012546 transfer Methods 0.000 description 1
- QORWJWZARLRLPR-UHFFFAOYSA-H tricalcium bis(phosphate) Chemical compound [Ca+2].[Ca+2].[Ca+2].[O-]P([O-])([O-])=O.[O-]P([O-])([O-])=O QORWJWZARLRLPR-UHFFFAOYSA-H 0.000 description 1
- 235000013311 vegetables Nutrition 0.000 description 1
- 235000020234 walnut Nutrition 0.000 description 1
Landscapes
- Medicinal Preparation (AREA)
Description
本発明は、優れた溶出速度をもたらし、経時安
定性に優れた固形製剤組成物に関するものであ
る。さらに詳しくいえば、少なくともβ−サイク
ロデキストリンと薬効成分の双方が、X線回折測
定により結晶性物質特有の回折ピークの存在を認
めなくなる程度に乾式混合粉砕処理しこれを錠
剤、カプセル剤、散剤、細粒剤、顆粒剤等に応用
するための固形製剤組成物に関するものである。
結晶セルロースと薬効成分を混合粉砕する方法
が、たとえば特開昭51−32718、51−32719により
開示されたが、当技術は固形製剤の溶出速度を高
め、生体における吸収を迅速かつ完全ならしめる
効果が製薬業界で注目されてきた。
この結晶セルロースと薬効成分の混合粉砕物か
ら得られる固形製剤は、優れた経時安定性、瞬時
の溶出性、かつin vivoにおける優れたアベイラ
ビリテイを示すことが種々の研究例から判明した
が、反面次のような欠陥を有していた。
すなわち、その効果を最大限に発揮するには、
混合粉砕時間を長くする必要があり、製剤の生産
効率上不利であるばかりでなく、場合により薬効
成分の劣化変質を招くおそれがあり好ましくなか
つた。
この問題を解決すべく、結晶セルロースの代り
にβ−サイクロデキストリンを用いる方法が提案
された。当社によれば、薬効成分との混合粉砕
は、結晶セルロースの場合よりも著しく短時間で
済ますことができる。しかしながら、β−サイク
ロデキストリンと薬効成分の混合粉砕物を製剤化
するには、大きな問題点があつた。
β−サイクロデキストリンと薬効成分の混合粉
砕物をそのまゝ圧縮成形して錠剤化することは、
成形性、流動性、滑沢性に乏しく困難であつた。
たとえ錠剤化されたとしても、その錠剤は錠剤硬
度等の物理的特性が経時的に変化して実用的では
なかつた。
β−サイクロデキストリンと薬効成分の混合粉
砕物を、カプセル製剤に応用することもまた困難
であつた。すなわち、混合粉砕物は極端に流動性
が悪く、また粘着性が発現してカプセル充填する
のが困難であつた。また流動性を与えるべく乾式
成形するには、前述したとおり成形性が悪く、粒
状化が困難であつた。
β−サイクロデキストリンと薬効成分の混合粉
砕物を、顆粒剤あるいは細粒剤に応用すること
も、造粒収率が悪く、また得られた顆粒剤、細粒
剤の粉化率が高くて実用的でなかつた。
β−サイクロデキストリンと薬効成分の混合粉
砕物を散剤に応用することも、特に流動性が悪い
ため分包時の計量バラツキが大きく、さらに服用
しにくいという問題点があつた。
以上のように、β−サイクロデキストリンと薬
効成分の混合粉砕物は、混合粉砕時間を短縮する
ことには貢献したが、実製剤に応用されるには、
その性能が不充分であつた。
本発明は、このような問題のあるβ−サイクロ
デキストリンと薬効成分の混合粉砕物の速溶出と
いう効果を維持しながら、実用特性と生産性の優
れた固形製剤の製造を可能にする固形製剤組成物
に関するものである。
まず、少なくともβ−サイクロデキストリンと
薬効成分を含む混合粉砕物を錠剤として応用する
場合、成形性、滑沢性、経時的安定性を賦与する
ために、賦形剤およびその他の製剤用添加剤を加
えることが必要である。こゝでいう賦形剤とは、
リン酸カルシウム、硫酸カルシウム、乳糖、白
糖、マンニツト、でんぷん、およびその誘導体な
どをさし、これらが単独もしくは組合せて使用さ
れる。
その他の製剤用添加剤とは、結合剤、滑沢剤、
流動剤などをさすが、結合剤としては、β−1・
4グルカンおよびその誘導体、たとえば、結晶セ
ルロース、セルロース粉末、カルボキシメチルセ
ルロースないしはそのナトリウム塩、ヒドロキシ
プロピルセルロース、メチルセルロース、ヒドロ
キシプロピルメチルセルロースなどがあり、さら
にポリビニルピロリドン、でんぷん誘導体類も利
用できる。これらはいずれも単独もしくは2個以
上組合せて使用される。
滑沢剤としては、ステアリルアルコール、ステ
アリン酸アルミニウム、ステアリン酸マグネシウ
ム、タルクなどがあり、流動剤としては、酸化マ
グネシウム、微粒子性酸化ケイ素、タルクなどが
あり、β−1・4グルカン、デンプンなどもこの
目的のために用いられることもある。
また、その他必要に応じて、カルボキシメチル
セルロースカルシウム塩、イオン交換樹脂などの
崩壊剤および着色剤、矯味剤などを使用できる。
少なくともβ−サイクロデキストリンと薬効成
分を含む混合粉砕物の錠剤化において加えられる
これら賦形剤およびその他の製剤用添加剤の量は
限定しえない。なぜならば、最終的製品である錠
剤1錠中の薬効成分量、錠剤1錠の重量などの条
件により処方が決定されるからである。しかし、
実用強度を維持し、経時的な錠剤品質の劣化を防
ぐには、結合剤量は、直打法の場合で10〜50重量
%、湿打法の場合で1〜30重量%が好ましい。
錠剤の製造は、直打法、湿打法ともに使用で
き、また通常の製錠条件と何ら変りなく製錠でき
る。このようにして得られた錠剤は、速やかな溶
出性と共に、優れた実用強度と崩壊性をもたら
し、さらに経時安定性も良好である。
次に、少なくともβ−サイクロデキストリンと
薬効成分を含む混合粉砕物をカプセル剤として応
用する場合、流動性、滑沢性を賦与するために、
流動剤および/または滑沢剤の添加が必要であ
る。また、乳糖、デンプン、結晶セルロースなど
の流動性のよい賦型剤、結合剤に、流動剤およ
び/または滑沢剤の一部または全部をおきかえて
もよい。また、その他、着色剤、矯味剤の添加も
自由である。
少なくともβ−サイクロデキストリンと薬効成
分を含む混合粉砕物のカプセル剤化において加え
られる製剤用添加剤の量は限定しえないが、たと
えば滑沢剤および/または流動剤の量は、0.2〜
3重量%が好ましい結果をもたらす。流動性のよ
い乳糖、デンプン、結晶セルロースなどの賦形
剤、結合剤で流動性、滑沢剤の機能を1部または
全部代替するには、5重量%以上の添加量を要す
る。
またカプセル製剤を粉末でなく顆粒状で行なう
場合の固形製剤組成は、錠剤のそれに準じて行な
えばよい。たゞし、この場合は、滑沢剤および/
または流動剤は必ずしも添加しなくてもよい。こ
のようにして得られたカプセル剤は、速やかな溶
出と共に均一な充填量をもつ。
少なくともβ−サイクロデキストリンと薬効成
分を含む混合粉砕物を顆粒剤あるいは細粒剤に応
用する場合、その製法が乾式法か湿式法かのいず
れにおいても、添加すべき賦形剤およびその他の
製剤用添加物およびその量は、錠剤化の場合と同
じである。たゞし、滑沢剤および/または流動剤
の添加は必ずしも必要ではない。このようにして
得られた顆粒剤あるいは細粒剤は、速やかな溶出
と共に、取扱、輸送等で粉末化しない適当な強度
を有する。さらに製造工程中で造粒収率が良いた
め経済的でもある。
少なくともβ−サイクロデキストリンと薬効成
分を含む混合粉砕物を散剤として応用する場合
は、流動剤の添加が必要である。また、乳糖、デ
ンプン、結晶セルロースなどの流動性のよい賦形
剤、結合剤に、流動性の一部または全部をおきか
えてよい。また矯味剤などの添加も自由である。
添加すべき流動剤の量を限定しえない理由は、錠
剤化の場合と同じであるが、目的とする流動性を
得るには、製剤用添加剤の量は5重量%以上が好
ましい。
このようにして得られた散剤は、速やかな溶出
と共に流動性がよいため、分包時の計量バラツキ
が少なく、服用しやすい。
少なくともβ−サイクロデキストリンと薬効成
分を含む混合粉砕物を各種固形製剤に応用する
際、製剤用添加剤としてβ−1・4グルカンを用
いることは極めて有効である。β−1・4グルカ
ンは結合剤として作用し、錠剤、顆粒剤、細粒
剤、カプセル剤の強度を高めると共に、流動性と
しての機能をも併せもつため、錠剤、カプセル
剤、散剤製造時においてもその有効性を発揮す
る。すなわち、少なくともβ−サイクロデキスト
リンと薬効成分の混合粉砕物を各種固形製剤に応
用する際の問題点を、製剤用添加剤としてβ−
1・4グルカンを使用することで解決できる場合
が多い。たとえば直打式錠剤製造において、β−
1・4グルカン以外の錠剤用添加剤を使用する場
合に比べて製剤用混合物の流動性が著しく改善さ
れ、錠剤の硬度も大巾に増大させることができ
る。
β−1・4グルカンの全組成物に対する含量
は、剤形すなわち錠剤か顆粒剤か細粒剤かカプセ
ル剤か散剤かによつても異なるし、薬効成分の種
類、量によつても異なるため一概にはいえない
が、通常、5〜50重量%が望ましい。5重量%よ
り少ない量では効果がうすく、50重量%より多く
しても、その改良効果の増加は小さい。
少なくともβ−サイクロデキストリンと薬効成
分を含む混合粉砕の実施において、β−サイクロ
デキストリンと薬効成分との混合比率は、限定す
ることが困難である。なぜならば、溶出速度をど
の程度にするかによつて混合比率を適宜選択でき
るからである。しかし、たとえば溶出速度を最大
にする必要がある場合は、β−サイクロデキスト
リン/薬効成分の重量比は40/60以上であること
が望ましい。これ以下では、溶出速度が低下する
傾向にあり望ましくない場合もある。
混合粉砕の実施は、少なくともβ−サイクロデ
キストリンと薬効成分から成ればよい。そして、
本発明でいう賦形剤およびその他の製剤用添加物
の添加は、混合粉砕時にβ−サイクロデキストリ
ンと薬効成分と共に加えてもよいし、あらかじめ
β−サイクロデキストリンと薬効成分を混合粉砕
した後で加えてもよい。前者は賦形剤およびその
他の製剤用添加物を後で加える手間が省きうると
いう利点をもち、後者は混合粉砕機器を小型化し
うるという利点をもつが、使用形態により自由に
使いわけられる。
賦形剤およびその他の製剤用添加物として、β
−1・4グルカンを使用する際は、このβ−1・
4グルカンの一部もしくは全部を、混合粉砕時に
β−サイクロデキストリンと主薬成分と共に加え
ることは有力な手段である。β−サイクロデキス
トリンとβ−1・4グルカンの相乗効果で、溶出
速度は一層高まる。さらにβ−1・4グルカンを
含まない混合粉砕物、すなわち、たとえばβ−サ
イクロデキストリンと薬効成分の混合粉砕物に比
べて吸湿性が低く、流動性のよい粉体を得ること
ができるし、粉砕の際、粉砕機器への付着、固着
を防止し、混合粉収率を上げることもできる。
β−サイクロデキストリンとβ−1・4グルカ
ンおよび薬効成分の混合粉砕物をそのまゝ、錠
剤、カプセル剤、顆粒剤、細粒剤、散剤に利用す
ることも可能であるが、さらに賦形剤その他の製
剤添加剤を添加することは望ましいことである。
たとえば直打法の錠剤化には、ステアリン酸金属
塩のごとき滑沢剤の添加は錠剤化作業を一層促進
するし、湿打法の錠剤化には、メチルセルロー
ス、ヒドロキシブロピルセルロースなどの添加が
有効である。またカプセル剤化においても、流動
剤および/もしくは滑沢剤の添加は、カプセル剤
の充填バラツキを一層低減させる。
また必要に応じて、賦形剤、矯味剤、崩壊剤、
着色剤の添加も自由である。
混合粉砕に用いる粉砕機器は、機械的に圧壊、
磨砕して微粒子化する機能を有するもので、たと
えば、回転ボールミル、振動ボールミル、ハンマ
ーミルなどが挙げられるが、水や溶媒の存在を必
要としないものであれば、その選択は自由であ
る。
混合粉砕の時間は、粉砕機の種類、試料量、粉
砕動力の大きさ等で変化するが、混合粉砕物のX
線回折測定により結晶性物質の特有な回折ピーク
の存在を認めなくなる程度行なう。それより適度
に混合粉砕を行なつても、エネルギー効率的にも
不利であり、薬効成分の変質をきたす場合もあり
うる。
本発明に応用される薬効成分は、水溶性、水難
溶性のいずれも利用できるが、水難溶性の薬効成
分の場合に特に本技術の利用効果が大である。こ
こでいう水難溶性とは、JPの通則21に示され
る表において、溶質1gを溶かすのに要する溶媒
(こゝでは水)量が30ml以上である薬効成分をさ
し、たとえば、カフエイン、カンフル、ジメルカ
プロール、フエノパルビタール、ピラビタール、
ジキトキシン、スルフイソキサゾール、アンピシ
リン、エリスロマイシン、キサタマイシン、クロ
ラムフエニコール、メチルテストステロン、フエ
ナセチン、テオフイリンなどがある。
本発明でいうサイクロデキストリンとは、たと
えば「食品と科学」4月号(1977)p97〜102に
詳述されるものであつて、Shardinger dextrinあ
るいはCycloamyloseとも呼ばれる環状オリゴ糖
同族体で、D−グルコースが6〜8個環状にα−
1・4結合した化合物であり、構成するグルコー
スの数により、α・β・γ−サイクロデキストリ
ンの分類される。本発明で最も効果的なのはβ−
サイクロデキストリンである。
本発明でいうβ−1・4グルカンとは、パル
プ、リンター、再生センイ等の植物性セルロース
原料を酸加水分解、アルカリ酸化分酸等の化学的
処理および/もしくは機械的粉砕処理することに
よつて得られるものをさす。
以下、実施例と共に本発明の効果について、そ
の詳細を説明する。
実施例 1
内容積5の磁製ボールミル(ボール径20〜30
mmφ、ボール個数20個、回転速度90rpm)に、局
方規格のフエナセチンを30g、β−サイクロデキ
ストリン〔安藤化成品(株)製〕を270gを入れて60
分間混合粉砕した(試料A)。
試料Aに1.5gのステアリン酸マグネシウムを
加えてポリ袋中で十分混合した後、断面積1cm2の
円筒型金型に入れて1錠500mgの錠剤を作成した
(成形圧力2ton/cm2)。当錠剤の木屋式硬度計によ
る錠剤硬度の測定結果は2Kg以下で、もろくて壊
れ易く実用的でなかつた(錠剤A−1)。
試料A100gに結晶乳糖(DMV150メツシユ)
を40g、結晶セルロース(旭化成製アビセルPH
−301)を60g、ステアリン酸マグネシウムを1
g添加して、ポリ袋中で十分混合した後、上述の
円筒型金型で圧縮成形した(成形圧力1ton/
cm2)。当錠剤の硬度は5〜6Kgで、JPによる崩
壊度の測定(純水、37±1℃、デイスクなし)結
果は、1分以内と速かであつた(錠剤A−2)。
錠剤A−1とA−2を40℃、75%RHの温湿度
条件下で2週間放置したところ、A−1はもろく
て、もはや指触にも耐えなかつたが、A−2は硬
度4〜5Kgであり、経時的変化はほとんど見られ
なかつた。
実施例 2
実施例1で述べた試料Aを多量に作成した。試
料Aを利用して表1および表2の処方により直打
錠および湿打錠を作成した。
直打錠は粉体混合を5容V型ブレンダーで30
分間行ない(仕込量500g)、ステアリン酸マグネ
シウムを外割りで0.5%相当量加えて、さらに10
分間混合した後、菊水製作所製RT−S9型錠剤機
(8mmφ、12R臼杵、錠剤重量200mg、打錠速度
18rpm)にて錠剤を作成した。
湿打錠はステアリン酸マグネシウムを除く原料
をV型ブレンダーで30分間混合した後(仕込量
500g)、5ニーダーに移し、3%メチルセルロ
ース糊液を適量加え(湿混練物がパサパサした状
態となる程度まで添加する)ながら20分間混合
し、フラツシユミル(不二パウダル製、スクリー
ン孔径3mmφ)にて湿式造粒し、60℃の熱風乾燥
機で8〜10時間乾燥して12メツシユ篩で篩過後、
ステアリン酸マグネシウムを外割りで0.5%加え
て混合し、直打錠と同様な条件で成形した。
このようにして得られた直打錠および湿打錠の
錠剤重量バラツキ(CV値)、錠剤硬度、錠剤崩壊
度、虐待試験後の錠剤硬度を測定した結果を表3
に示した。
The present invention relates to a solid dosage composition that provides an excellent dissolution rate and excellent stability over time. More specifically, at least both the β-cyclodextrin and the medicinal ingredient are dry mixed and crushed to such an extent that the presence of diffraction peaks characteristic of crystalline substances is no longer recognized by X-ray diffraction measurement, and the mixture is processed into tablets, capsules, powders, etc. The present invention relates to a solid pharmaceutical composition for application to fine granules, granules, etc. A method of mixing and pulverizing crystalline cellulose and medicinal ingredients has been disclosed, for example, in JP-A No. 51-32718 and 51-32719, but this technology has the effect of increasing the dissolution rate of solid preparations and ensuring rapid and complete absorption in the body. has been attracting attention in the pharmaceutical industry. Various studies have shown that solid preparations obtained from this pulverized mixture of crystalline cellulose and medicinal ingredients exhibit excellent stability over time, instantaneous dissolution, and excellent availability in vivo. It had defects such as: In other words, to maximize its effectiveness,
It is necessary to increase the mixing and pulverizing time, which is not only disadvantageous in terms of production efficiency of the preparation, but also undesirable because it may lead to deterioration and alteration of the medicinal ingredients in some cases. In order to solve this problem, a method using β-cyclodextrin instead of crystalline cellulose was proposed. According to our company, mixing and grinding with medicinal ingredients can be completed in a significantly shorter time than in the case of crystalline cellulose. However, there were major problems in formulating a pulverized mixture of β-cyclodextrin and medicinal ingredients. Compression molding of the pulverized mixture of β-cyclodextrin and medicinal ingredients to form tablets is as follows:
This was difficult due to poor moldability, fluidity, and smoothness.
Even if it were made into a tablet, the physical properties of the tablet, such as tablet hardness, changed over time, making it impractical. It has also been difficult to apply a pulverized mixture of β-cyclodextrin and medicinal ingredients to capsule formulations. That is, the mixed pulverized product had extremely poor fluidity and developed stickiness, making it difficult to fill into capsules. Furthermore, when dry molding is performed to impart fluidity, the moldability is poor as described above, and granulation is difficult. Applying a pulverized mixture of β-cyclodextrin and medicinal ingredients to granules or fine granules has a poor granulation yield, and the powdering rate of the resulting granules and fine granules is too high for practical use. It didn't make sense. Application of a pulverized mixture of β-cyclodextrin and medicinal ingredients to a powder has also had the problem of poor fluidity, which results in large variations in measurements during packaging, and furthermore makes it difficult to take. As mentioned above, the pulverized mixture of β-cyclodextrin and medicinal ingredients has contributed to shortening the mixing and pulverization time, but it is difficult to apply it to actual preparations.
Its performance was insufficient. The present invention provides a solid preparation composition that enables the production of solid preparations with excellent practical properties and productivity while maintaining the effect of rapid dissolution of a mixed pulverized mixture of β-cyclodextrin and medicinal ingredients, which has been problematic. It is about things. First, when a pulverized mixture containing at least β-cyclodextrin and a medicinal ingredient is applied as a tablet, excipients and other formulation additives are added to impart formability, smoothness, and stability over time. It is necessary to add. The excipients mentioned here are
It refers to calcium phosphate, calcium sulfate, lactose, sucrose, mannitrate, starch, and derivatives thereof, and these may be used alone or in combination. Other formulation additives include binders, lubricants,
It refers to flow agents, etc., but as a binder, β-1・
4-glucan and its derivatives, such as crystalline cellulose, cellulose powder, carboxymethyl cellulose or its sodium salt, hydroxypropyl cellulose, methyl cellulose, and hydroxypropyl methyl cellulose, and polyvinylpyrrolidone and starch derivatives can also be used. Any of these may be used alone or in combination of two or more. Lubricants include stearyl alcohol, aluminum stearate, magnesium stearate, talc, etc. Glidants include magnesium oxide, particulate silicon oxide, talc, etc. β-1.4 glucan, starch, etc. Sometimes used for this purpose. In addition, disintegrants such as carboxymethylcellulose calcium salts and ion exchange resins, coloring agents, and flavoring agents can be used as necessary. There is no limit to the amount of these excipients and other pharmaceutical additives added in tabletting the mixed pulverized product containing at least β-cyclodextrin and a medicinal active ingredient. This is because the prescription is determined by conditions such as the amount of medicinal ingredients in one tablet, which is the final product, and the weight of one tablet. but,
In order to maintain practical strength and prevent deterioration of tablet quality over time, the amount of binder is preferably 10 to 50% by weight in the case of the direct compression method, and 1 to 30% by weight in the case of the wet compression method. Both the direct compression method and the wet compression method can be used to manufacture the tablets, and the tablets can be manufactured under the same conditions as normal tablet manufacturing. The tablets thus obtained have rapid dissolution properties, excellent practical strength and disintegration properties, and also have good stability over time. Next, when applying the pulverized mixture containing at least β-cyclodextrin and medicinal ingredients as a capsule, in order to impart fluidity and smoothness,
Addition of flow agents and/or lubricants is necessary. Further, part or all of the flow agent and/or lubricant may be replaced with a filler or binder having good fluidity such as lactose, starch, or crystalline cellulose. In addition, coloring agents and flavoring agents may also be added freely. Although there is no limit to the amount of pharmaceutical additives added in encapsulating the mixed pulverized product containing at least β-cyclodextrin and a medicinal ingredient, for example, the amount of a lubricant and/or flow agent may be from 0.2 to
3% by weight gives favorable results. In order to replace part or all of the fluidity and lubricant functions with excipients and binders such as lactose, starch, and crystalline cellulose that have good fluidity, an amount of 5% by weight or more is required. Furthermore, when preparing a capsule preparation in the form of granules rather than powder, the composition of the solid preparation may be made in accordance with that of tablets. However, in this case, the lubricant and/or
Alternatively, a flow agent may not necessarily be added. The capsules thus obtained have a uniform filling volume with rapid dissolution. When a pulverized mixture containing at least β-cyclodextrin and a medicinal ingredient is applied to granules or fine granules, whether the manufacturing method is a dry method or a wet method, excipients to be added and other preparations are required. The additives and their amounts are the same as for tabletting. However, the addition of lubricants and/or flow agents is not always necessary. The granules or fine granules thus obtained have rapid dissolution and adequate strength to prevent pulverization during handling, transportation, etc. Furthermore, it is economical because the granulation yield is good during the manufacturing process. When applying a pulverized mixture containing at least β-cyclodextrin and a medicinal ingredient as a powder, it is necessary to add a flow agent. Further, part or all of the fluidity may be replaced by an excipient or binder with good fluidity such as lactose, starch, or crystalline cellulose. Additionally, flavoring agents and the like can be added freely.
The reason why the amount of flow agent to be added cannot be limited is the same as in the case of tabletting, but in order to obtain the desired flowability, the amount of the additive for formulation is preferably 5% by weight or more. The powder thus obtained has rapid dissolution and good fluidity, so there is little variation in measurements during packaging and it is easy to take. When applying a pulverized mixture containing at least β-cyclodextrin and a medicinal ingredient to various solid preparations, it is extremely effective to use β-1,4 glucan as an additive for the preparation. β-1.4 glucan acts as a binder, increasing the strength of tablets, granules, fine granules, and capsules, and also has a fluidity function, so it is used during the production of tablets, capsules, and powders. also demonstrates its effectiveness. In other words, at least the problems when applying a pulverized mixture of β-cyclodextrin and medicinal ingredients to various solid preparations can be solved by using β-cyclodextrin as an additive for formulations.
The problem can often be solved by using 1.4 glucan. For example, in direct compression tablet manufacturing, β-
Compared to the case of using tablet additives other than 1,4-glucan, the fluidity of the formulation mixture is significantly improved, and the hardness of the tablets can also be greatly increased. The content of β-1.4 glucan in the total composition varies depending on the dosage form, i.e., tablet, granule, fine granule, capsule, or powder, as well as the type and amount of medicinal ingredient. Although this cannot be said unconditionally, it is usually desirable that the content be 5 to 50% by weight. If the amount is less than 5% by weight, the effect will be weak, and if the amount is more than 50% by weight, the increase in the improvement effect will be small. In carrying out mixing and pulverization containing at least β-cyclodextrin and medicinal ingredients, it is difficult to limit the mixing ratio of β-cyclodextrin and medicinal ingredients. This is because the mixing ratio can be appropriately selected depending on the elution rate. However, if, for example, it is necessary to maximize the dissolution rate, it is desirable that the weight ratio of β-cyclodextrin/medicinal ingredient is 40/60 or more. Below this range, the elution rate tends to decrease, which may be undesirable. Mixing and pulverization may be carried out as long as the mixture consists of at least β-cyclodextrin and a medicinal ingredient. and,
The excipients and other pharmaceutical additives referred to in the present invention may be added together with β-cyclodextrin and the medicinal ingredient during mixing and pulverization, or they may be added after the β-cyclodextrin and medicinal ingredient have been mixed and pulverized in advance. It's okay. The former has the advantage of eliminating the need to add excipients and other pharmaceutical additives later, and the latter has the advantage of making mixing and grinding equipment more compact, but they can be used freely depending on the form of use. As excipients and other formulation additives, β
When using -1.4 glucan, this β-1.
An effective method is to add part or all of the 4-glucans together with β-cyclodextrin and the main drug ingredient during mixing and pulverization. The synergistic effect of β-cyclodextrin and β-1,4 glucan further increases the elution rate. Furthermore, it is possible to obtain a powder mixture that does not contain β-1,4 glucan, that is, a powder with lower hygroscopicity and better fluidity than, for example, a mixture pulverization product of β-cyclodextrin and a medicinal ingredient. At this time, it is possible to prevent adhesion and sticking to the grinding equipment and increase the yield of mixed powder. Although it is possible to use the pulverized mixture of β-cyclodextrin, β-1,4 glucan, and medicinal ingredients as it is in tablets, capsules, granules, fine granules, and powders, it is also possible to use excipients. It may be desirable to add other formulation additives.
For example, when making tablets using the direct compression method, the addition of a lubricant such as metal stearate further facilitates the tabletting process, and when making tablets using the wet compression method, the addition of methylcellulose, hydroxypropyl cellulose, etc. is recommended. It is valid. Also in encapsulation, the addition of flow agents and/or lubricants further reduces filling variations in capsules. In addition, excipients, flavoring agents, disintegrants,
Coloring agents can also be added freely. The crushing equipment used for mixed crushing is mechanically crushing,
It has the function of grinding into fine particles, such as a rotary ball mill, a vibrating ball mill, a hammer mill, etc., but the choice is free as long as it does not require the presence of water or a solvent. The time for mixed pulverization varies depending on the type of pulverizer, the amount of sample, the size of the pulverizing power, etc.
Linear diffraction measurements are carried out to such an extent that the presence of diffraction peaks characteristic of crystalline substances is no longer recognized. Even if the mixture is mixed and pulverized more appropriately, it is disadvantageous in terms of energy efficiency and may cause deterioration of the medicinal ingredients. The medicinal ingredients applied to the present invention can be either water-soluble or poorly water-soluble, but the present technology is particularly effective in the case of sparingly water-soluble medicinal ingredients. Here, poorly water-soluble refers to medicinal ingredients that require 30 ml or more of solvent (water in this case) to dissolve 1 g of solute in the table shown in JP General Rules 21, such as caffeine, camphor, dimercaprol, phenoparbital, pyravital,
These include diquitoxin, sulfisoxazole, ampicillin, erythromycin, xatamycin, chloramphenicol, methyltestosterone, phenacetin, and theophylline. Cyclodextrin as used in the present invention is a cyclic oligosaccharide homolog also called Shardinger dextrin or cycloamylose, which is described in detail in, for example, "Food and Science" April issue (1977), p. 97-102, and is 6 to 8 α-
It is a compound with 1 and 4 bonds, and is classified into α, β, and γ-cyclodextrins depending on the number of constituent glucose molecules. The most effective in the present invention is β-
It is a cyclodextrin. In the present invention, β-1,4 glucan is obtained by subjecting vegetable cellulose raw materials such as pulp, linter, and recycled walnuts to acid hydrolysis, chemical treatment such as alkali oxidation, and/or mechanical crushing treatment. Refers to what you can get. Hereinafter, the effects of the present invention will be explained in detail along with Examples. Example 1 Porcelain ball mill with internal volume of 5 (ball diameter 20 to 30
mmφ, number of balls: 20, rotation speed: 90 rpm), add 30 g of pharmacopoeial standard phenacetin and 270 g of β-cyclodextrin [manufactured by Ando Kasei Co., Ltd.], and add 60 g of
Mixed and ground for minutes (sample A). 1.5 g of magnesium stearate was added to Sample A, thoroughly mixed in a plastic bag, and then placed in a cylindrical mold with a cross-sectional area of 1 cm 2 to form tablets each weighing 500 mg (molding pressure 2 ton/cm 2 ). The tablet hardness of this tablet measured using a Kiya hardness tester was 2 kg or less, indicating that it was brittle and easily broken, making it impractical (Tablet A-1). Crystalline lactose (DMV150 mesh) to 100g of sample A
40g, crystalline cellulose (Asahi Kasei Avicel PH
-301) 60g, magnesium stearate 1
After mixing thoroughly in a plastic bag, compression molding was performed in the above-mentioned cylindrical mold (molding pressure 1 ton/mold).
cm2 ). The hardness of this tablet was 5 to 6 kg, and the degree of disintegration measured by JP (pure water, 37±1°C, no disk) was as fast as within 1 minute (tablet A-2). When tablets A-1 and A-2 were left for two weeks under the temperature and humidity conditions of 40℃ and 75%RH, A-1 was brittle and could no longer withstand the touch, but A-2 had a hardness of 4. The weight was ~5Kg, and almost no change over time was observed. Example 2 Sample A described in Example 1 was prepared in large quantities. Using sample A, direct compression tablets and wet compression tablets were prepared according to the formulations shown in Tables 1 and 2. For direct compression tablets, mix the powder with a 5-volume V-type blender to make 30 tablets.
1 minute (prepared amount: 500 g), add magnesium stearate in an amount equivalent to 0.5%, and then add 100 g of magnesium stearate.
After mixing for a minute, use a Kikusui Seisakusho RT-S9 tablet machine (8 mmφ, 12R punch, tablet weight 200 mg, tableting speed).
Tablets were prepared at 18 rpm). Wet tablets are made by mixing the raw materials except magnesium stearate in a V-type blender for 30 minutes.
500g), transferred to a kneader 5, mixed for 20 minutes while adding an appropriate amount of 3% methylcellulose paste (add until the wet kneaded material becomes dry), and then using a flat mill (manufactured by Fuji Powdal, screen pore size 3 mmφ). Wet granulate, dry in a hot air dryer at 60℃ for 8 to 10 hours, and pass through a 12-mesh sieve.
Magnesium stearate was added in an amount of 0.5% and mixed, and molded under the same conditions as direct compression tablets. Table 3 shows the results of measuring the tablet weight variation (CV value), tablet hardness, tablet disintegration degree, and tablet hardness after abuse test of the directly compressed tablets and wet compressed tablets obtained in this way.
It was shown to.
【表】【table】
【表】【table】
【表】【table】
【表】
実施例 3
実施例1の方法に準じて、β−サイクロデキス
トリン、スルフイソキサゾール(山之内製薬製)
の6:4混合物を混合粉砕した。得られた混合粉
砕物(試料B)に、乳糖(DMV100メツシユ)
0、5、10、20%となるような量を添加して、ス
テアリン酸マグネシウムを外割りで1%加え、V
型ブレンダーで20分間混合した後、ザナシ式カプ
セル充填機LZ−64型により3号カプセルに充填
し、充填重量バラツキを調査した。結果を表4に
示す(たゞし、空カプセル重量は差し引いた)。[Table] Example 3 According to the method of Example 1, β-cyclodextrin, sulfisoxazole (manufactured by Yamanouchi Pharmaceutical Co., Ltd.)
A 6:4 mixture of was mixed and ground. Lactose (DMV100 mesh) was added to the obtained mixed pulverized product (sample B).
0, 5, 10, 20%, add 1% of magnesium stearate, V
After mixing in a mold blender for 20 minutes, the mixture was filled into No. 3 capsules using a Zanasi capsule filling machine model LZ-64, and variations in filling weight were investigated. The results are shown in Table 4 (the empty capsule weight was subtracted).
【表】
なお、C−1処方は長時間運転しているとカプ
セル充填機のスピンドルに付着し、スムーズな運
転を妨げた。
実施例 4
スルフイソキサゾール、β−サイクロデキスト
リン、結晶セルロース(旭化成製アビセルPH−
101)の3者を、実施例1に準じてボールミルに
て混合粉砕した(配合処方を表5に示す)。たゞ
し、G−16〜G−18は結晶セルロースを含まな
い。また表5の備考欄に混合粉砕後の粉体の外観
の観察結果を示した。得られた粉砕物に、乳糖
(DMV150メツシユ)、結晶セルロースおよびカル
ボキシメチルセルロース・カルシウムをそれぞれ
表6のとおり加え、5容V型ブレンダーにて20
分間混合し、ステアリン酸カルシウムを加えて8
分間混合した後、実施例2の方法に準じて直打し
た。[Table] In addition, the C-1 formulation adhered to the spindle of the capsule filling machine when operated for a long time, hindering smooth operation. Example 4 Sulfisoxazole, β-cyclodextrin, crystalline cellulose (Asahi Kasei Avicel PH-
101) were mixed and ground in a ball mill according to Example 1 (the blending recipe is shown in Table 5). However, G-16 to G-18 do not contain crystalline cellulose. In addition, the observation results of the appearance of the powder after mixing and pulverization are shown in the remarks column of Table 5. Lactose (DMV 150 mesh), crystalline cellulose, and carboxymethylcellulose/calcium were added to the obtained pulverized material as shown in Table 6, and blended in a 5-volume V-type blender for 20 min.
Mix for 8 minutes and add calcium stearate.
After mixing for a minute, it was directly pounded according to the method of Example 2.
【表】【table】
【表】
表6で得られた錠剤をU.S.P.規格の回転バスケ
ツト法により溶出速度を測定した(溶出媒:
水)。液温を37±1℃に調節し、一定時間毎に被
検液2ml(G−1、G−2、G−16は1ml)を
取し、100ml容メスフラスコに移す。0.1N−
NaOH0.5mlを加えた後、純水で100mlとし、20分
間放置後、波長253nmにて紫外吸収を測定し、
その吸光度より検量線法にしたがつて溶出量を求
めた。その結果を表7に示した。[Table] The dissolution rate of the tablets obtained in Table 6 was measured by the rotating basket method according to USP standards (dissolution medium:
water). Adjust the liquid temperature to 37±1°C, and take 2 ml of the test liquid (1 ml for G-1, G-2, and G-16) at regular intervals and transfer it to a 100 ml volumetric flask. 0.1N−
After adding 0.5 ml of NaOH, the volume was made up to 100 ml with pure water, and after being left for 20 minutes, the ultraviolet absorption was measured at a wavelength of 253 nm.
The elution amount was determined from the absorbance according to the calibration curve method. The results are shown in Table 7.
【表】
実施例 5
抗生物質のクロラムフエニコール(日本薬局方
規定品)100mgとβ−サイクロデキストリン900mg
を、ステンレス製シエーカーミル(柳本製作所)
に封入して粉砕した。粉砕条件は、内容積80c.c.、
ボール数17個、ボール径11mmである。粉砕時間は
6時間であつた。予備実験の結果から、X線回折
図がクロラムフエニコールおよびβ−サイクロデ
キストリンの双方とも結晶性ピークを示さなくな
るまでの時間を採つた。
X線回折法の測定条件の一例を述べれば以下の
とおりである。
測定条件:[Table] Example 5 Antibiotic chloramphenicol (Japanese Pharmacopoeia prescribed product) 100mg and β-cyclodextrin 900mg
A stainless steel sheaker mill (Yanagimoto Seisakusho)
It was sealed and crushed. The grinding conditions are: internal volume 80c.c.
There are 17 balls and a ball diameter of 11 mm. The grinding time was 6 hours. Based on the results of the preliminary experiment, the time until the X-ray diffraction diagram showed no crystalline peaks for both chloramphenicol and β-cyclodextrin was measured. An example of measurement conditions for the X-ray diffraction method is as follows. Measurement condition:
【表】
装置:
X線回折装置は、理学電気製自記X線回折装置
Mode D−3F型を用いた。
得られた混合粉砕物50重量部に結晶乳糖50重量
部を加え散剤を作成した。この散剤の溶出速度は
10分後で70%、60分後で100%であり、流動性は
良好で分包時のバラツキが少なかつたが、乳糖を
含まない系は分包時のバラツキが大であつた。
実施例 6
表8に示す配合で混合粉砕を行ない、実施例8
に準じて製剤を行なつた。なお、比較を厳密に行
なうため、錠剤成形圧力をコントロールして16〜
20分間で崩壊するような錠剤を作成し、その溶出
速度を測定した。測定結果を表9に示す。[Table] Equipment: The X-ray diffraction equipment is a self-recording X-ray diffraction equipment manufactured by Rigaku Denki.
Mode D-3F type was used. 50 parts by weight of crystalline lactose was added to 50 parts by weight of the obtained mixed pulverized product to prepare a powder. The dissolution rate of this powder is
It was 70% after 10 minutes and 100% after 60 minutes, indicating good fluidity and little variation during packaging, but the lactose-free system had large variations during packaging. Example 6 Mixing and pulverization were carried out with the formulation shown in Table 8, and Example 8
The formulation was carried out according to the following. In order to make a strict comparison, the tablet forming pressure was controlled and
Tablets that disintegrated in 20 minutes were prepared and the dissolution rate was measured. The measurement results are shown in Table 9.
【表】
を加えて混合した。
[Table] was added and mixed.
【表】【table】
【表】
る。
なお、No.7、No.8は成形性が乏しく、もろい
錠剤しかできなかつたが、No.1〜No.6は高硬度
の錠剤を与えた。No.7、No.8でしつかりした錠
剤をつくるには、直打法であれば結晶セルロース
などの、湿打法であれば適当量の賦形剤および結
合剤の添加を必要とする。
実施例 7
内容積5の磁性ボールミル(ボール径20〜30
mmφ、ボール個数20個、回転速度80rpm)に、局
方規格のフエナセチン30gを入れ、β−サイクロ
デキストリンまたはβ−1・4グルカン〔旭化成
工業(株)製「アビセル」PH−101〕270gを加えて
3時間混合粉砕し、それぞれ試料Mおよび試料N
を得た。
実施例5で示したX線回折測定条件でX線回折
図を書かせると、試料Mでは結晶性物質に固有な
回折ピークの消失が観測されたが、試料Nでは、
結晶性回折ピーク、特に結晶セルロースのそれが
強く残つていた。
試料Mまたは試料Nを80重量%、ステアリン酸
マグネシウムを0.5重量%、β−1・4グルカン
(同「アビセル」PH−302)を19.5重量%配合
し、ポリ袋中で十分混合した後、断面積1cm2の円
筒形金型で1錠500mgの錠剤を作成した(成形圧
力1.5ton/cm2)。錠剤物性の評価結果を表10に、溶
出速度評価結果を表11に示す。[Table]
Note that No. 7 and No. 8 had poor moldability and could only yield brittle tablets, but No. 1 to No. 6 gave highly hard tablets. To make firm tablets with No. 7 and No. 8, it is necessary to add appropriate amounts of excipients and binders, such as crystalline cellulose if using the direct compression method, or appropriate amounts of excipients and binders when using the wet compression method. Example 7 Magnetic ball mill with internal volume 5 (ball diameter 20-30
mmφ, 20 balls, rotation speed 80 rpm), put 30 g of pharmacopoeial standard phenacetin, and add 270 g of β-cyclodextrin or β-1,4 glucan [“Avicel” PH-101 manufactured by Asahi Kasei Corporation]. Sample M and Sample N were mixed and ground for 3 hours.
I got it. When an X-ray diffraction diagram was drawn under the X-ray diffraction measurement conditions shown in Example 5, the disappearance of the diffraction peak unique to crystalline substances was observed in Sample M, but in Sample N,
Crystalline diffraction peaks, especially those of crystalline cellulose, remained strong. A mixture of 80% by weight of sample M or sample N, 0.5% by weight of magnesium stearate, and 19.5% by weight of β-1,4 glucan (Avicel PH-302) was thoroughly mixed in a plastic bag and then cut. Tablets each weighing 500 mg were prepared using a cylindrical mold with an area of 1 cm 2 (molding pressure of 1.5 ton/cm 2 ). The evaluation results of tablet physical properties are shown in Table 10, and the evaluation results of dissolution rate are shown in Table 11.
【表】【table】
【表】
実施した。
以上の結果から明らかなとおり、β−サイクロ
デキストリンを混合粉砕時に添加したものは、従
来のβ−1・4グルカン系よりも短時間で望むべ
き発明効果が得られ、の混合粉砕試料に、別途製
剤用添加剤としてβ−1・4グルカンを添加して
錠剤化したものは、十分な実用強度を与え、溶出
速度も初期から大きく、かつ虐待試験後の錠剤物
性変化も小さかつた。
実施例 8
表12の配合処方粉体をそれぞれ1gずつ、ステ
ンレス製シエーカーミル(柳本製作所)に封入し
て粉砕した。粉砕条件は、内容積80c.c.、ボール数
17個、ボール径11mmであり、粉砕時間は、1時
間、3時間、6時間、12時間であつた。粉砕後、
それぞれの試料を、実施例5に示したX線回折測
定条件でX線回折を行ない。混合粉砕時間の長短
に関する評価を行なつた。[Table] Implemented.
As is clear from the above results, the desired inventive effect can be obtained in a shorter time than the conventional β-1,4-glucan system when β-cyclodextrin is added at the time of mixing and pulverization. Tablets prepared by adding β-1,4 glucan as a formulation additive gave sufficient strength for practical use, had a high dissolution rate from the initial stage, and showed little change in the physical properties of the tablets after the abuse test. Example 8 1 g of each powder with the formulation shown in Table 12 was placed in a stainless steel sheaker mill (Yanagimoto Seisakusho) and pulverized. The grinding conditions are: internal volume 80 c.c., number of balls.
There were 17 balls with a diameter of 11 mm, and the grinding times were 1 hour, 3 hours, 6 hours, and 12 hours. After crushing,
Each sample was subjected to X-ray diffraction under the X-ray diffraction measurement conditions shown in Example 5. The length of mixing and grinding time was evaluated.
【表】
スルフイソキサゾール単独系およびスルフイソ
キサゾール/β−1・4グルカン混合系が、X線
回折ピークを失うのに長時間必要なのに比べて、
β−サイクロデキストリンが処方された系は、明
らかに迅速な混合粉砕効果が現われた。
6時間粉砕試料1部に、乳糖1部、結晶セルロ
ース1部、ステアリン酸マグネシウム0.03部を加
え、十分混合後、実施例7の方法で錠剤とした
後、実施例4に示した溶出速度測定条件(ただ
し、回転バスケツトを用いず、バドル法を採用)
で、溶出速度を評価した。[Table] Compared to the sulfisoxazole single system and the sulfisoxazole/β-1,4 glucan mixed system, it takes a long time to lose the X-ray diffraction peak.
The system formulated with β-cyclodextrin clearly showed a rapid mixing and grinding effect. Add 1 part of lactose, 1 part of crystalline cellulose, and 0.03 part of magnesium stearate to 1 part of the 6-hour pulverized sample, and after thorough mixing, form tablets by the method of Example 7, and then apply the dissolution rate measurement conditions shown in Example 4. (However, the paddle method is used instead of a rotating basket)
The elution rate was evaluated.
【表】
No.2、No.3のβ−サイクロデキストリンを含
む処方は、溶出速度が大であつた。[Table] The formulations containing β-cyclodextrin No. 2 and No. 3 had a high dissolution rate.
Claims (1)
成分および製剤用添加剤からなり、少なくともβ
−サイクロデキストリンと水難溶性の薬効成分の
双方が、X線回折測定により結晶性物質特有の回
折ピークの存在を認めなくなる程度に乾式混合粉
砕されていることを特徴とする固形製剤組成物。 2 製剤用添加剤がβ−1・4グルカンである特
許請求の範囲第1項記載の固形製剤組成物。 3 β−1・4グルカンの含量が全組成物に対し
て5〜50重量%である特許請求の範囲第2項記載
の固形製剤用組成物。 4 β−1・4グルカンがβ−サイクロデキスト
リンと薬効成分と共に混合粉砕されている特許請
求の範囲第2項記載の固形製剤組成物。 5 製剤用添加剤がβ−1・4グルカンと他の製
剤用添加剤からなり、β−1・4グルカンがβ−
サイクロデキストリンと薬効成分と共に混合粉砕
されている特許請求の範囲第1項記載の固形製剤
組成物。[Scope of Claims] 1 Consists of β-cyclodextrin, a poorly water-soluble medicinal ingredient, and a pharmaceutical additive;
- A solid pharmaceutical composition characterized in that both cyclodextrin and a sparingly water-soluble medicinal ingredient are dry mixed and pulverized to such an extent that the presence of diffraction peaks characteristic of crystalline substances is no longer observed by X-ray diffraction measurements. 2. The solid pharmaceutical composition according to claim 1, wherein the pharmaceutical additive is β-1,4 glucan. 3. The composition for solid preparation according to claim 2, wherein the content of β-1.4 glucan is 5 to 50% by weight based on the total composition. 4. The solid pharmaceutical composition according to claim 2, wherein β-1.4 glucan is mixed and ground together with β-cyclodextrin and a medicinal ingredient. 5 The pharmaceutical additive consists of β-1,4 glucan and other pharmaceutical additives, and β-1,4 glucan consists of β-1,4 glucan.
The solid pharmaceutical composition according to claim 1, which is mixed and ground together with cyclodextrin and a medicinal ingredient.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP15433077A JPS5486607A (en) | 1977-12-23 | 1977-12-23 | Solid pharmaceutical composition |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP15433077A JPS5486607A (en) | 1977-12-23 | 1977-12-23 | Solid pharmaceutical composition |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS5486607A JPS5486607A (en) | 1979-07-10 |
| JPS6137247B2 true JPS6137247B2 (en) | 1986-08-22 |
Family
ID=15581780
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP15433077A Granted JPS5486607A (en) | 1977-12-23 | 1977-12-23 | Solid pharmaceutical composition |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS5486607A (en) |
Families Citing this family (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| PH20837A (en) * | 1983-04-29 | 1987-05-08 | Pennwalt Corp | Rapid dissolving uniform drug compositon |
| US4616008A (en) * | 1984-05-02 | 1986-10-07 | Takeda Chemical Industries, Ltd. | Antibacterial solid composition for oral administration |
| JPS6272688A (en) * | 1985-09-25 | 1987-04-03 | Ss Pharmaceut Co Ltd | Tipepidine citrate-containing composition |
| WO1988003023A1 (en) * | 1986-10-31 | 1988-05-05 | Mitsubishi Chemical Industries Limited | Drug composition for treating liver diseases and process for its preparation |
| YU45837B (en) * | 1988-01-18 | 1992-07-20 | LEK TOVARNA FARMACEVTSKIH IN KEMIČKIH IZDELKOV d.d. | PROCEDURE FOR PREPARATION OF THE NEW NICARDIPINE INCLUSION COMPLEX OZ. ITS HYDROCHLORIDE WITH BETA-CYCLODEXTRIN |
| MX2008011418A (en) * | 2006-03-06 | 2008-09-22 | Teva Pharma | Ezetimibe compositions. |
| JP2009091309A (en) * | 2007-10-10 | 2009-04-30 | Japan Organo Co Ltd | Composition containing bacopa monniera extract and its manufacturing method, as well as drinks and foods |
| JP4890657B1 (en) * | 2011-06-03 | 2012-03-07 | 小野薬品工業株式会社 | Tablet containing Limaprost and β-cyclodextrin |
-
1977
- 1977-12-23 JP JP15433077A patent/JPS5486607A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS5486607A (en) | 1979-07-10 |
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