TW200816998A - Process for preparing pramipexole dihydrochloride tablets - Google Patents
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- A61P25/14—Drugs for disorders of the nervous system for treating abnormal movements, e.g. chorea, dyskinesia
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Abstract
Description
200816998 九、發明說明: 【發明所屬之技術領域】 本叙明係關於一種製備普拉克素(pramipex〇le)二氫氯化 物錠劑之方法。詳言之,本發明係關於一種製備普拉克素 二氫氯化物錠劑之方法,其中該等錠劑呈現高儲存穩定 性。 【先前技術】200816998 IX. DESCRIPTION OF THE INVENTION: TECHNICAL FIELD OF THE INVENTION This description relates to a method of preparing a pramipex〇le dihydrochloride tablet. In particular, the present invention relates to a process for preparing a pluconin dihydrochloride tablet wherein the tablets exhibit high storage stability. [Prior Art]
晋拉克素為—種已知之多巴胺02受體促效劑。其在結構 上不同於源於麥角之藥物(例如,溴麥角環肽(bromocriptine) 或培高利特(pergolide))。其在藥理學上亦為獨特的,原因 在於其為完全促效劑且對多巴胺受體之多巴胺於家族具有 受體選擇性。普拉克素最初揭示於美國專利第4,731,374 號、第4,如,_號及第4,886,812號中,所有專利以引用的 方式併入本文中。 在化學上將普拉克素命名為 于P石馮(S)-2-胺基-4,5,6,7-四氫-6- (丙胺基)苯幷噻唑,且苴且右八 一 一有刀子式C丨oHnls^S及相對分子 貝里2 1 1 · 3 3。化學式係如下所示:Jinlaqin is a known dopamine 02 receptor agonist. It is structurally different from the drug derived from ergot (for example, bromocriptine or pergolide). It is also pharmacologically unique because it is a fully agonist and has receptor selectivity for the dopamine receptor dopamine family. Plaques are disclosed in U.S. Patent Nos. 4,731,374, 4, the disclosures of which are incorporated herein by reference. Chemically named plucometer as P von (S)-2-amino-4,5,6,7-tetrahydro-6-(propylamino)benzothiazole, and 右 right 八一There are knife type C丨oHnls^S and relative molecular Bailey 2 1 1 · 3 3 . The chemical formula is as follows:
〇 通常使用之溶劑合物形式為並 八工m U 飞馬日拉克素二氫氯化物單水合 物(刀子式CioHnChNgOs ;相對八曰 + -气畜仆舲口口 P人 對刀子貝置302.27)。普拉克 素一虱虱化物早水合物為白 ^ 5 外 巳至灰白色、無味結晶粉末。 在296 C至301C之範圍内 生烙融,同時發生分解。普拉 123707.doc 200816998 克素為具有-個對掌中心之對拿性化合物。純⑻·對映異 構體係自合成方法藉由在合成期間中間物中之一者進行對 掌性再結晶獲得。 普拉克素二氫氯化物單水合物為一種高度可溶之化合 物。水溶解度大於2Gmg/mL,且在緩衝介f中之溶解度在 2與阳7·4之間時一般在1〇叫就之上。普拉克素二氯 氯化物單水合物不具有吸濕性,且具有高結晶性。在研磨 I,結晶變體(單水合物)不發生改變。普拉克素處於固態 時非常穩定,然而處於溶液狀態時其具有光敏性。 普拉克素速釋(IR)錠劑首先在1997年於USA得到核准, 在隨後幾年時間内接著在歐盟(EU)、瑞士、加拿大及南美 洲以及在東歐、近東及亞洲國家得到上市核准。 在EU及US,指示普拉克素IR錠劑用於與左旋多巴 (Levodopa)組合來治療早期巴金森氏病(parkins〇n,s Disease) 或晚期巴金森氏病之徵象及症狀。該產品在us A以商標名 MIRAPEX®而為人所知。指示一天服用IR錠劑三次。 2005年在USA上市之普拉克素二氫氯化物單水合物旋劑 (下文中將上市包裝/產品稱為"商品調配物”)的製造方法產 生具有相對穩定存放期之錠劑,其中在儲存〗8個月後大致 95%之標示平均量的活性成份仍存在於錠劑中。然而,需 要開發在儲存很長時間後具有盡可能接近於零降解之產 品。 本發明係關於一種製備普拉克素二氫氯化物單水合物錠 劑之方法,其中該等錠劑呈現高儲存穩定性。 123707.doc 200816998 【發明内容】 為達成本揭示案及本發明之㈣,下文中術語”普拉克 素鼠氯化物思谓晋拉克素二氫氯化物及其醫藥學上可 接受之溶劑合物,特別包括普拉克素二氫氯化物單水合 物。 根據本發明,提供—種生產普拉克素二氫氯化物錠劑之 方法,其中該等錠劑呈現高儲存穩定性。 另外提供一種製備普拉克素二氫氯化物錠劑之方法,其 中該方法涉及調配包含粒内製錠成份、普拉克素二氫氯: 物、黏合劑及粒外製錠劑之H該方法包含以下步驟: 視U况將粒内製紅成份按大小分選(size)以形成大小大體 上均一之粒内製錠成份顆粒,形成包含該等視情況大小大 體上均一之粒内製錠成份、普拉克素二氫氯化物及黏合劑 的預此物’將該預混物製成顆粒,且將該粒狀預混物乾燥 至約1.5%至約2.5%,更佳h〇%至約2 5%之終點水分含量 以形成乾燥預混物,將粒外製錠劑與乾燥預混物混合以形 成最終摻混物,及將該最終摻混物壓縮成錠劑。 進一步提供一種製備包含粒内製錠成份、普拉克素二氫 氯化物、黏合劑及粒外製錠劑之普拉克素二氫氯化物旋劑 之方法,纟中該方法之至少一部分係在一封閉系統中進行 且包含以下步驟: (a)將粒内製錠成份之顆粒裝入流化床製粒機中,其中 粒内製錠成份之顆粒可視情況在裝入前按大小分選以形 成大小大體上均一之顆粒,且將該等成份混合, 123707.doc 200816998 (b) 將普拉克素二氫氯化物及聚乙烯吡咯酮溶解於水中 以形成普拉克素二氫氯化物水溶液,且將該普拉克素二 氫氯化物溶液喷灑於該流化床製粒機中的粒内製錠成份 顆粒上, (c) 製備黏合劑糊狀物及/或糊狀懸浮液及/或懸浮液, 且藉由噴灑將該黏合劑糊狀物及/或糊狀懸浮液及/或懸 浮液添加至流化床製粒機中以形成顆粒, (d) 將該粒狀混合物乾燥至約1〇%至約2·5%之終點水分 含量, (e) 視情況將乾燥顆粒通過篩分研磨機以形成原料顆 粒, ⑴將步驟⑷之該粒狀預混物與粒外製鍵劑混合,及摻 混以形成最終摻混物, (g)使用製錠機將該最終摻混物壓縮成錠劑。 兑在-較佳實施例中,提供—種製備包含粒内製鍵成份、 普拉克素二氫氯化物、黏合劑及粒外製It劑之普拉克素二 氫氯化物錠劑之太、、表,甘士 ^ & Μ您方法,其中該方法之至少一部分係在一封 閉系統中進行且包含以下步驟: (步驟D =甘露糖醇、無水膠狀二氧切及玉米殿粉裝入 二化床製粒機中’其中粒内製錠成份之顆粒可視 ^况在裝入珂按大小分選以形成大小大體上均一 顆粒’且將該等成份混合,較佳為乾燥混合 物, (步驟2)將普拉身 凡畜一虱鼠化物溶解於水及聚乙烯吡咯酮 123707.doc 200816998 中以形成普拉克素二氫氯化物水溶液,且將該普 拉克素一氫氯化物溶液噴灑於該流化床製粒機中 的粒内製錠成份顆粒上, (步驟3 )製備縣法> 、心予於、、,屯水中之玉米澱粉糊狀物,且將該糊 狀物添加至流化床製粒機中以形成顆粒(流化床製 粒),同時較佳使濕顆粒避光。 (v驟4)乾知顆粒’較佳同時使乾燥顆粒避光。 (步驟5)藉由篩分研磨機通過乾燥顆粒來製備原料顆粒; (父1 )藉:於擴散混合器將該原料顆粒與硬脂酸鎂、無 水膠狀二氧化珍及玉米殿粉摻混(最終摻混物)。 〇驟7)將該最終摻混物壓製成具有最終強度之錠劑(錠 劑),例如,約21〇 mg。 (步驟8)視情況進行包裝。 根據上逑方法及其實施例生產之鍵劑呈現高儲存穩定性 屬性。 本發明之另一態樣包括一種製造包含普拉克素二氫氯化 =樂錠劑調配物之方法,其中在饥及6〇%相對濕度 =存條件下18個月時仍存在於鍵劑中之普拉克素二氫氯 勿的平均量為標示量之至少約97°/。。 、 物另一態樣包括一種製造包含普拉克素二氯氯化 酉錢劑調配物之方法,其中在抑及6()%相對濕度 化:勿件:24個月時仍存在於錠劑中之普拉克素二氫氯 约均量為標示量之至少約95%,且另外可能較 至少約97%。 123707.doc 200816998 本發明之另-態樣包括一種製造包含普拉克素二氫氯化 物之醫藥㈣1調配物之方法’其中在饥及㈣相對渴度 之儲存條件下36個月時仍存在於錢劑中之普拉克素二氮氯〇 The form of the solvate usually used is 八工m U feiqi eric acid dihydrochloride monohydrate (knife type CioHnChNgOs; relative gossip + - gas servant mouth mouth P person pair knife set 302.27) . The pramid- sulphide early hydrate is a white 5 巳 to an off-white, odorless crystalline powder. In the range of 296 C to 301 C, it melts and melts at the same time. Pula 123707.doc 200816998 Is a compound with a pair of palms. The pure (8)·enantiomer system self-synthesis method is obtained by performing palmar recrystallization on one of the intermediates during the synthesis. Plasmin dihydrochloride monohydrate is a highly soluble compound. The water solubility is greater than 2 Gmg/mL, and the solubility in the buffer medium f is generally between 1 and 77. Plazisine dichloride chloride monohydrate is not hygroscopic and has high crystallinity. In the grinding I, the crystal modification (monohydrate) did not change. Plasm is very stable in the solid state, but it is photosensitive in the solution state. The Plaques immediate release (IR) lozenges were first approved in the USA in 1997 and subsequently approved for marketing in the European Union (EU), Switzerland, Canada and South America, as well as in Eastern Europe, Near East and Asia. In EU and US, the Plaques IR lozenge is used in combination with Levodopa to treat signs and symptoms of early Parkinsin's disease, or late Parkinson's disease. This product is known under the trade name MIRAPEX® in us A. Indications to take IR tablets three times a day. The manufacturing method of the Platinol dihydrochloride monohydrate spinner (hereinafter referred to as the "packaged product/product called "commodity formulation") marketed in the USA in 2005 produces a tablet having a relatively stable shelf life, wherein Storage: Approximately 95% of the indicated average amount of active ingredient is still present in the tablet after 8 months. However, it is necessary to develop a product that is as close as possible to zero degradation after a long period of storage. The present invention relates to a preparation A method of lacrin dihydrochloride monohydrate tablet wherein the tablet exhibits high storage stability. 123707.doc 200816998 SUMMARY OF THE INVENTION To achieve the present disclosure and (4) of the present invention, the term "Plack" The squirrel chloride is a sulphate dihydrochloride and a pharmaceutically acceptable solvate thereof, and particularly includes prasin dihydrochloride monohydrate. According to the present invention, there is provided a method of producing a pramin dihydrochloride tablet wherein the tablets exhibit high storage stability. Further provided is a method for preparing a plucometer dihydrochloride tablet, wherein the method comprises formulating H comprising an intragranular tableting component, a plucometer dihydrochloride: a binder, an extragranular tableting agent, and the method comprises The following steps: Depending on the U condition, the intra-granular red component is sized to form granules of substantially uniform size in the granules, forming an intragranular tablet containing substantially uniform size, Pre-mixing of the plucan dihydrochloride and the binder', the premix is granulated, and the granulated premix is dried to about 1.5% to about 2.5%, more preferably 〇% to about 2 An end point moisture content of 5% to form a dry premix, the extragranular tableting agent is mixed with the dry premix to form the final blend, and the final blend is compressed into a tablet. Further provided is a method for preparing a plucometer dihydrochloride spinning agent comprising an intragranular tableting component, a plucometer dihydrochloride, a binder, and an extragranular tableting agent, wherein at least a portion of the method is The closed system is carried out and comprises the following steps: (a) loading the granules of the granulated tablet component into a fluidized bed granulator, wherein the granules of the granulated tablet component are optionally sorted by size before being charged to form Particles of substantially uniform size and mixing of the ingredients, 123707.doc 200816998 (b) Dissolving plucan dihydrochloride and polyvinylpyrrolidone in water to form an aqueous solution of plucan dihydrochloride, and Spraying the plucometer dihydrochloride solution onto the granules of the granules in the fluidized bed granulator, (c) preparing a binder paste and/or a paste suspension and/or suspension And adding the binder paste and/or paste suspension and/or suspension to the fluidized bed granulator by spraying to form granules, (d) drying the granulated mixture to about 1 Torr. % to about 2.5% of the endpoint moisture content, (e) as appropriate The dried granules are passed through a sieving mill to form raw material granules, (1) the granulated premix of step (4) is mixed with an extragranular bonding agent, and blended to form a final blend, (g) using a tablet machine The final blend is compressed into a tablet. In a preferred embodiment, a method for preparing a plucometer dihydrochloride tablet containing an intragranular bond component, a plucometer dihydrochloride, a binder, and an extragranular It agent is provided. Table, Gans ^ & Μ your method, wherein at least part of the method is carried out in a closed system and comprises the following steps: (Step D = mannitol, anhydrous gelatinous dioxygen cut and corn powder into two In a chemical granulator, the granules of the granules in the granules can be sorted according to the size of the granules to form substantially uniform granules, and the components are mixed, preferably a dry mixture, (step 2 Dissolving the pus-mouse compound in water and polyvinylpyrrolidone 123707.doc 200816998 to form an aqueous solution of plucan dihydrochloride, and spraying the plucometer-hydrochloride solution on the stream On the intragranular tablet component particles in the chemical granulator, (Step 3) prepare a corn starch paste of the county method, the heart, and the water, and add the paste to the fluidization. In a bed granulator to form granules (fluidized bed granulation), the same Preferably, the wet granules are protected from light. (v. 4) The granules are preferably 'while keeping the dry granules away from light. (Step 5) The raw granules are prepared by drying the granules by a sieving mill; (Father 1) By: The raw material granules are mixed with magnesium stearate, anhydrous colloidal oxidized sulphuric acid and corn house powder in a diffusion mixer (final blend). Step 7) Pressing the final blend into an ingot having a final strength The agent (tablet), for example, is about 21 mg. (Step 8) Pack as appropriate. The key agent produced according to the above method and its embodiment exhibits a high storage stability property. Another aspect of the invention includes a method of making a formulation comprising a plucometer dihydrochlorination = lozenge formulation, wherein it is still present in the bonding agent at 18 months of hunger and 6% relative humidity = storage conditions The average amount of plucan dihydrochloride is at least about 97 °/ of the indicated amount. . Another aspect of the invention includes a method of making a formulation comprising a plucometer dichlorochloride, wherein the inhibition is 6 ()% relative humidity: no part: 24 months still present in the tablet The average amount of plucan dihydrogen chloride is at least about 95% of the indicated amount, and may be at least about 97%. 123707.doc 200816998 Another aspect of the invention includes a method of making a pharmaceutical (4) 1 formulation comprising pramidin dihydrochloride, which is still present in money under 36 months of hunger and (four) relative thirst storage conditions Plasmidine dinitrochloride
化物的平均量為標示量之牵♦的Q 里又至夕約95%,且另外可能較佳為 至少約97%。 如本文所使用之術語,,平均量"係藉由測定存在於具體產 物樣品中之指定產物(活性成份或降解產物)的量及接著取 參 產物樣品的平均值來計算。 通常在最終普拉克素商品中,以包裝產品形式包括錠 劑,且包裝可包括瓶、發泡包裝或其類似物。 根據以下揭示内容,本發明之該等及其他特徵、益處及 優勢將顯而易見。 【實施方式】 根據本發明’可製備呈現高儲存穩定性之普拉克素二氣 氯化物㈣1 °此在製藥界係有價值的,原因在於其使藥: 製造商能夠生產普拉克素二氫氣化物錠劑且將其長期儲 存’因此減少了關於產品是否已超過其有效期及是否需要 處理之擔憂。此又使藥房且最終使消f者能夠享受到與需 要監測藥品之功效及需要因產品到期而補充市有: 之成本降低的益處。 關 根據本發明,已發現藉由在製造普拉克素二氫氯化物錠 劑期間控制某些參數,所得錠劑呈現高穩定性。詳言之, 控制粒内製錠成份之粒徑以使其具有相對大體均二可 選)、製備及使用黏合劑懸浮液、在—封㈣統中進行该 123707.doc 200816998 方法以及在製錠前控制產物之水分含量使得能夠生產具有 非常理想之儲存穩定性提高的普拉克素二氫氯化物錠劑。 根據以上所述,本發明之普拉克素二氫氯化物錠劑包含 粒内製錠成份、普拉克素二氫氯化物、黏合劑及粒外製鍵 齊卜本發明方法包含以下步驟:將粒内製錠成份按大小分 t X开/成大小大體上均一之粒内製錠成份顆粒(可選步 • 驟)’形成&含視情況大小均—之粒内製鍵成份、普拉克 素二氫氣化物及黏合劑之混合物’將該混合物製成顆粒, 且將該㈣大混合物乾燥至約! 〇%至約2 5%之終點水分含量 (乾秌失重(LOD),在95-l〇5°C下,較佳在1〇5〇c下)以形成 乾燥混合物,將粒外製錠劑與該乾燥混合物混合以形成最 終摻混物’及㈣最終摻混物壓縮成鍵劑。&另一實施例 中’將粒狀混合物乾燥至約15%至約25%之終點水分含 量。 圖1闡明-種調配錠劑之方法,其可產生具有高穩定性 # 曰拉克素商σ口。圖1中所示之方法涉及-種製備包含粒 内I叙成知、晋拉克素二氫氯化物、黏合劑及粒外製旋劑 之普拉克素二氫氯化物錠劑之方法,其中該方法之至少一 冑分係在-封閉系統中進行。該方法包含以下步驟: U)將粒内製!定成份之顆粒裝人流化床製粒機中,其中 粒内製鍵成份之顆粒可視情況在裝入前按大小分選以形 成大小大體上均一之顆粒, ㈠將日ϋ t素—氫氯化物及聚乙烯,卜各酮溶解於水中 X H拉克素_氫氣化物水溶液,且將該普拉克素二 123707.doc 200816998 氫氯化物溶液噴灑於該流化床製粒機中的粒内製錠成份 顆粒上, (0製備黏合劑糊狀物及/或糊狀懸浮液及/或懸浮液, 且藉由喷灑將黏合劑懸浮液添加至流化床製粒機中, (d)在流化床製粒機中將粒内製錠成份顆粒、普拉克素 一氫氯化物溶液及黏合劑溶液混合以形成混合物, 0)將該混合物製成顆粒以形成粒狀混合物, (f) 將該粒狀混合物乾燥至約1.0%至約2·5%之終點水分 含量, (g) 將步驟(f)之該粒狀混合物與粒外製錠劑混合,及換 混以形成最終摻混物, (h) 使用製錠機將該最終摻混物壓縮成錠劑。 粒内製紅成份包括甘露糖醇USP、膠狀二氧化石夕 NF、聚乙烯吡咯酮(K25)USP、玉米澱.NF及純水usp。 在本發明方法中用作起始物質之甘露醇_D較佳為δ結晶 受體與β結晶變體之混合物。較佳地,g結晶變體之重量百 分比大於β結晶變體之重量百分比。較佳地,β結晶變體之 百分比不大於10%,其餘90%為δ結晶變體。在一實施例 中’ β δ里係在1 · 0 %與1 0 %之間,較佳在1 · 5 %與1 〇 %之間, 更佳在2.0%與10%之間,且甚至更佳在25%與1〇%之間。 本發明之粒外製錠劑包括膠狀二氧化矽NF '玉求殿粉 NF及硬脂酸鎂NF。 就粒内製錠成份及粒外製錠成份而言,下表以用於各批 中之總量的百分比形式給出各錠劑中製錠成份之較佳量以 123707.doc -12- 200816998 及API(晋拉克素二氫氯化物)之量 表1 成份 甘露糖醇 玉米 硬脂j|多The average amount of the compound is about 95% of the Q of the labeled amount, and may additionally be at least about 97%. As used herein, the term "average amount" is calculated by determining the amount of a specified product (active ingredient or degradation product) present in a particular product sample and then taking the average of the sample of the product. Typically in the final plucani commercial product, the tablet is included in the form of a packaged product, and the package may comprise a bottle, a blister pack or the like. These and other features, advantages and advantages of the present invention will be apparent from the <RTIgt; [Embodiment] According to the present invention, it is possible to prepare a plucometer dichloride chloride (IV) exhibiting high storage stability. This is valuable in the pharmaceutical industry because it enables the manufacturer to produce pramidin dihydrogenate. Lozenges and their long-term storage' thus reduce concerns about whether the product has exceeded its expiration date and whether it needs to be disposed of. This in turn allows the pharmacy and ultimately the consumer to enjoy the benefits of having to monitor the efficacy of the drug and the need to supplement the market due to product expiration: According to the present invention, it has been found that the resulting tablet exhibits high stability by controlling certain parameters during the manufacture of the plucometer dihydrochloride tablet. In particular, the particle size of the ingot component is controlled to be relatively large and uniform, the preparation and use of the binder suspension, the method of the 123707.doc 200816998 and the method before the ingot preparation are carried out. Controlling the moisture content of the product enables the production of a plucometer dihydrochloride tablet having an extremely desirable increase in storage stability. According to the above, the plucometer dihydrochloride tablet of the present invention comprises an intragranular tableting component, a plucometer dihydrochloride, a binder, and an extragranular bond. The method of the present invention comprises the following steps: Ingredients in the ingots are divided into the size of the size of the X. The size of the ingots is generally uniform. The ingot particles (optional step) 'formation & Mixture of dihydrogen compound and binder 'This pellet is granulated and the (4) large mixture is dried to about! 〇% to about 25% of the endpoint moisture content (dry weight loss (LOD), at 95-l〇5 ° C, preferably at 1〇5〇c) to form a dry mixture, the extragranular tableting agent Mixing with the dry mixture to form the final blend' and (iv) final blending is compressed into a bonding agent. & In another embodiment, the particulate mixture is dried to an endpoint moisture content of from about 15% to about 25%. Figure 1 illustrates a method of formulating a tablet which produces a high stability #曰拉克素商 σ mouth. The method illustrated in Figure 1 relates to a method of preparing a plucometer dihydrochloride tablet comprising an intragranular I, a sulphate dihydrochloride, a binder, and an extragranular spirulina, wherein At least one of the methods is performed in a closed system. The method comprises the following steps: U) granules! In the granule-loaded fluidized bed granulator, the granules of the granules in the granules may be sorted by size before being charged to form granules of substantially uniform size. (1) The ruthenium-hydrochloride And the polyethylene, the ketone is dissolved in water XH laccase-hydrogenated water solution, and the pramin II 123707.doc 200816998 hydrochloride solution is sprayed into the fluidized bed granulator On the granules, (0) prepare a binder paste and/or a paste suspension and/or suspension, and add the binder suspension to the fluidized bed granulator by spraying, (d) in the fluidization In the bed granulator, the intragranular tablet component particles, the plucometer-hydrochloride solution and the binder solution are mixed to form a mixture, 0) the mixture is granulated to form a granulated mixture, (f) the granule The mixture is dried to an endpoint moisture content of from about 1.0% to about 2.5%, (g) the particulate mixture of step (f) is mixed with the extragranular tableting agent, and the mixture is recombined to form the final blend, ( h) Compressing the final blend into a tablet using a tablet machine. Intragranular red components include mannitol USP, colloidal silica dioxide NF, polyvinylpyrrolidone (K25) USP, corn starch, NF and pure water usp. The mannitol_D used as a starting material in the process of the invention is preferably a mixture of a delta crystalline acceptor and a beta crystalline variant. Preferably, the weight percentage of the g crystal modification is greater than the weight percentage of the beta crystal modification. Preferably, the percentage of beta crystal modifications is no more than 10% and the remaining 90% is a delta crystalline variant. In one embodiment, 'β δ is between 1·0% and 10%, preferably between 1.7 % and 1%, more preferably between 2.0% and 10%, and even more Good between 25% and 1%. The extragranular tableting agent of the present invention comprises colloidal cerium oxide NF 'Yuqiudian powder NF and magnesium stearate NF. For the intragranular tablet component and the extragranular tablet component, the following table gives the preferred amount of the tablet component in each tablet as a percentage of the total amount used in each batch to 123707.doc -12- 200816998 And API (Zilacin dihydrochloride) scale 1 ingredient mannitol corn stearin j|
API 一 ________^_ * * A PI (遂' i 卜 曰 京二氳氯化物)之量視所要錠劑強度而定 旋劑強度可A A T,c 為0.125 mg至2.5 mg,其中典型強度為〇,125 § 0 25 叫、G.5G mg、G·75 mg、1 mg、ι·5 mg及 2·〇 mg 〇 下表給出夕種錠劑調配物,其為本發明之錠劑調配物的 代表性實例而非限制性實例: 表2 組份API ________^_ * * A PI (遂' i 曰 曰 氲 氲 氲 氲 氲 之 之 i i i i i i i i 旋 旋 旋 旋 旋 旋 旋 旋 旋 旋 旋 旋 旋 旋 旋 旋 旋 旋 旋 旋 旋 旋 旋 旋 旋 旋 旋 旋 旋, 125 § 0 25 叫, G.5G mg, G·75 mg, 1 mg, ι·5 mg, and 2·〇mg 〇 The following table gives the formulation of the lozenge formulation, which is the tablet formulation of the present invention. Representative examples of non-limiting examples: Table 2 Components
API 亳克/録:劑 0.125 玉米殿粉,經乾燥 玉米殿粉,未經乾燥 膠狀二氧化矽 49.455 ^-_—25.〇1〇 7.300 聚乙烯吼咯g同(Kj^ 硬脂酸鎂 0.940 1.230 1.15 L50 2.3 2,35 3.10 4.00 4.0API 亳克/录: agent 0.125 corn house powder, dried corn house powder, undried gelatinous cerium oxide 49.455 ^-_-25. 〇1 〇 7.300 polyethylene 吼 g g (Kj^ magnesium stearate 0.940 1.230 1.15 L50 2.3 2,35 3.10 4.00 4.0
純水係根據所使用之設備而調適,且不出 123707.doc 甘露糖醇 0.940 0,25 61.00 30.90 9.00 1.20 0.5 1.00 1.25 122.0 61.8 18.0 2.4 121.50 61.85 18.00 2.30 162.00 82.55 24.00 3.10 1.5 208.5 106.0 30.8 4.0 -13- 200816998 現在最終產物中。 鍵:=發Γ法來生產本發明之普拉克素二氫氯化物 β U勢包括②儲存穩定性。料高儲存 包括(但不必限於)長存放期。 〜 根據本發明方法製備之普拉克素二氫氯化物錠劑的 放期係由錠劑當在特定條件下儲存時保持高^ 成份的能力來呈現。 之/舌性 誶言之’根據本發明方法製備之普拉克素二氫氣化物錠 劑在25°c及60%相斟、月由 L乳化物叙 料度之樂條件下18個科仍存在於 叙财之普拉克素二氯氯化物的平均量為標示量之至少約 平。I :存在相同條件下之商品調配物平均值小於標示量 w、句里:)之95·8/〇。存在於根據本發明製備之儲存旋劑中 之活f生成h的里之時間趨勢㈣响可預計達24個月且甚至 達36個月,盆中其召* 甚至在36個月時將仍存在大於標示量之 95%。此當缺音羞舌 1B 田—義重大’原因在於其允許產品之長存放 且因此為消費者節省費用,因為該產品不必因製造 銷商及/或藥師儲存之未用產品到期而過於頻繁地 由衣造商更換。 以下實例為用於根據本發明製備普拉克素脫水物旋劑之 代表性方法。 實例2 乂下方法係用於製備〇·5 mg普拉克素二氫氯化物錠劑: ^米内成知在通過具有_篩網之comil(Qiiadro) 的同時分配至流化床製粒機中: 123707.doc 200816998 甘露糖醇-D: 122,000 g ㈣二氧化石夕: 1,200 g 玉米殿粉’經乾燥(未經乾燥)·· 565000(58,800)g 友在一獨立不鏽鋼容器中,在攪拌下將500 g普拉克素二 氫氯化物單水合物溶解於2G,_如純水中,且接著在授掉 下添加2,300 g聚維㈣(聚乙烯Dfcn各酮κ25),且溶解至完 全。接著將普拉克素二氫氯化物溶液噴灑於流化床製粒機 中之粒内成份混合物上。在一獨立不鏽鋼容器中,在攪拌 下將5,800 g乾;^玉米殿粉(未經乾燥者為⑽〇心添加至 ’ 〇 ml、、’屯水中’形成澱粉糊狀物。接著將澱粉糊狀物添 加至已加熱至95t之38,_ m丨純水中,且以自約州卿 起之速率㈣(㈣可為約㈣卿至約125G RPM)e接著 1力另外21,000 ml純水(室溫),且以35〇 授摔。使溫 度冷卻至約6代(在該階段溫度可為約饥至約饥)。 著將澱粉溶液噴灑於流化床製粒機中的粒内成份與普拉克 素二氫氯化物之混合物上。接著將流化床製粒機中之物質 製成I粒,且乾燥至2.3%之殘餘水分含量,且經由筛分研 磨機筛分以形成普拉克素原料顆粒。在擴散混合器中以10 RPM將硬脂酸鎂(3,咖g)、膠狀:氧切U,· g)及玉米 澱:⑴糊g)之粒外摻混物與187,_ §普拉克素原料顆 粒此合30分鐘以形成最終摻混物。接著將最終換混物壓縮 成重210mg且含有〇.5mg普拉克素二氫氯化物之旋劑。 本發明之料並不受本文所述之意欲作為本發明個別態 樣之早純說明的特定實施例限制,且功能上均等之方法及 123707.doc 200816998 組份係在本發明之範疇内。實際上,對熟習此項技術者而 言’根據以上描述及隨附圖式,除本文展示且描述之彼等 外的本發明之各種修改將變得顯而易見。該等修改意欲屬 於隨附申請專利範圍之範疇。 【圖式簡單說明】 圖1為展示根據本發明之 物錠劑之方法的流程圖。 恶樣生產普拉克素二氫氯化The pure water system is adapted according to the equipment used, and does not produce 123707.doc mannitol 0.940 0,25 61.00 30.90 9.00 1.20 0.5 1.00 1.25 122.0 61.8 18.0 2.4 121.50 61.85 18.00 2.30 162.00 82.55 24.00 3.10 1.5 208.5 106.0 30.8 4.0 -13 - 200816998 Now in the final product. Key: = Hairpin method to produce the pramin dihydrochloride of the present invention The β U potential includes 2 storage stability. High storage includes, but is not limited to, long shelf life. ~ The expiration of the plucometer dihydrochloride tablet prepared according to the method of the present invention is exhibited by the ability of the tablet to maintain a high content when stored under specific conditions. / Tongue rumors 'The plucan dihydrogenate tablets prepared according to the method of the present invention are still present in 18 families under the condition of 25 ° C and 60% phase 斟, month L emulsifier The average amount of prasin dichloride is less than about the amount indicated. I: The average value of the commodity formulation under the same conditions is less than the labeled amount w, 95:8/〇 in the sentence:). The time trend (4) of the activity f generated in the storage agent prepared according to the present invention can be expected to be 24 months and even 36 months, and the call in the pot will still exist even at 36 months. More than 95% of the indicated amount. The reason for this is that the vocal vocal 1B field is significant because the product allows for long storage of the product and therefore saves the consumer because the product does not have to be too frequent due to expiration of unused products stored by the manufacturer and/or pharmacist. The ground is replaced by a clothing manufacturer. The following examples are representative methods for preparing a plucometer dehydrating agent in accordance with the present invention. Example 2 The underarm method was used to prepare a 〇·5 mg pramin dihydrochloride tablet: ^Minaizhi was dispensed into a fluidized bed granulator while passing through a coil (Qiiadro) with a sieve: 123707.doc 200816998 Mannitol-D: 122,000 g (4) Dioxide Day: 1,200 g Corn House Powder 'Dryed (not dried) · · 565000 (58,800) g Friends in a separate stainless steel container, under stirring 500 g of pramidin dihydrochloride monohydrate was dissolved in 2G, such as pure water, and then 2,300 g of poly (iv) (polyethylene Dfcn each ketone κ25) was added and allowed to dissolve to completion. The plucometer dihydrochloride solution is then sprayed onto the intragranular component mixture in the fluid bed granulator. In a separate stainless steel container, 5,800 g of dry; ^ corn house powder (not dried (10) 〇 heart added to ' 〇 ml, ' '屯 water' to form a starch paste. Then the starch paste Add to the 38, _ m丨 pure water that has been heated to 95t, and at a rate from the state of the state (four) ((4) can be about (four) qing to about 125G RPM) e then 1 force another 21,000 ml of pure water (room Warm), and 35 〇 drop. Allow the temperature to cool to about 6 generations (the temperature can be about hunger to about hunger at this stage). The intragranular composition of the starch solution sprayed in the fluidized bed granulator A mixture of laccase dihydrochloride. The material in the fluidized bed granulator is then made into I pellets and dried to a residual moisture content of 2.3% and sieved through a sieve mill to form a pramin material. Granules. Extragranular blends of magnesium stearate (3, g), colloidal: oxygen cut U, g) and corn starch: (1) paste g) at 10 RPM in a diffusion mixer with 187, _ § Plaques raw material pellets for 30 minutes to form the final blend. The final blend was then compressed to a weight of 210 mg and containing 0.55 mg of palladium dihydrochloride. The present invention is not limited by the specific examples described herein, which are intended to be purely illustrative of the individual aspects of the present invention, and functionally equivalent methods and 123707.doc 200816998 components are within the scope of the present invention. In fact, various modifications of the invention in addition to those which are shown and described herein will be apparent. Such modifications are intended to fall within the scope of the accompanying claims. BRIEF DESCRIPTION OF THE DRAWINGS Fig. 1 is a flow chart showing a method of a lozenge according to the present invention. Production of plucan dihydrochlorination
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RU (1) | RU2009110253A (en) |
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WO (1) | WO2008023027A2 (en) |
Families Citing this family (15)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US8518926B2 (en) | 2006-04-10 | 2013-08-27 | Knopp Neurosciences, Inc. | Compositions and methods of using (R)-pramipexole |
ATE537826T1 (en) | 2006-05-16 | 2012-01-15 | Knopp Neurosciences Inc | COMPOSITIONS OF R(+)- AND S(-)-PRAMIPEXOLE AND METHOD FOR THEIR USE |
US8524695B2 (en) | 2006-12-14 | 2013-09-03 | Knopp Neurosciences, Inc. | Modified release formulations of (6R)-4,5,6,7-tetrahydro-N6-propyl-2,6-benzothiazole-diamine and methods of using the same |
EP2137171A4 (en) | 2007-03-14 | 2010-05-19 | Knopp Neurosciences Inc | Synthesis of chirally purified substituted benzothiazole diamines |
US20080254117A1 (en) * | 2007-04-10 | 2008-10-16 | Noel Cotton | Process for preparing pramipexole dihydrochloride tablets |
US20110190356A1 (en) | 2008-08-19 | 2011-08-04 | Knopp Neurosciences Inc. | Compositions and Methods of Using (R)- Pramipexole |
TR200906997A1 (en) * | 2009-09-11 | 2011-03-21 | Sanovel �La� San. Ve T�C. A. �. | Pramipexole pharmaceutical compositions. |
EP2462925A1 (en) | 2010-11-12 | 2012-06-13 | Neuraxpharm Arzneimittel GmbH | Pramipexole Dihydrochloride Granulate |
KR101712049B1 (en) * | 2010-11-17 | 2017-03-03 | 엘지이노텍 주식회사 | Light emitting device |
US9512096B2 (en) | 2011-12-22 | 2016-12-06 | Knopp Biosciences, LLP | Synthesis of amine substituted 4,5,6,7-tetrahydrobenzothiazole compounds |
US9662313B2 (en) | 2013-02-28 | 2017-05-30 | Knopp Biosciences Llc | Compositions and methods for treating amyotrophic lateral sclerosis in responders |
US9468630B2 (en) | 2013-07-12 | 2016-10-18 | Knopp Biosciences Llc | Compositions and methods for treating conditions related to increased eosinophils |
RS61539B1 (en) | 2013-07-12 | 2021-04-29 | Knopp Biosciences Llc | Treating elevated levels of eosinophils and/or basophils |
ES2813674T3 (en) | 2013-08-13 | 2021-03-24 | Knopp Biosciences Llc | Compositions and methods for treating plasma cell disorders and b-cell prolymphocytic disorders |
CA2921381A1 (en) | 2013-08-13 | 2015-02-19 | Knopp Biosciences Llc | Compositions and methods for treating chronic urticaria |
Family Cites Families (8)
Publication number | Priority date | Publication date | Assignee | Title |
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EP0998933A1 (en) * | 1998-10-09 | 2000-05-10 | Boehringer Mannheim Gmbh | Process for producing pharmaceutical compositions containing diphosphonates for oral administration |
ES2197600T3 (en) * | 1999-01-29 | 2004-01-01 | Disphar International B.V. | PHARMACEUTICAL COMPOSITIONS. |
BR0215262A (en) * | 2001-12-20 | 2004-12-28 | Pharmacia Corp | Zero-order sustained release dosage forms and manufacturing process |
US7749533B2 (en) * | 2003-05-07 | 2010-07-06 | Akina, Inc. | Highly plastic granules for making fast melting tablets |
CN101005830B (en) * | 2004-08-13 | 2010-09-29 | 贝林格尔·英格海姆国际有限公司 | Extended release tablet formulation containing pramipexole or a pharmaceutically acceptable salt thereof, method for manufacturing the same and use thereof |
NZ553645A (en) * | 2004-08-13 | 2010-09-30 | Boehringer Ingelheim Int | Extended release pellet formulation containing pramipexole or a pharmaceutically acceptable salt thereof, method for manufacturing the same and use thereof |
JP4446177B2 (en) * | 2005-01-21 | 2010-04-07 | 東和薬品株式会社 | Method for producing moisture-resistant orally disintegrating tablets |
JP2009519970A (en) * | 2005-12-15 | 2009-05-21 | アキュスフィア, インコーポレイテッド | Process for producing particle-based pharmaceutical dosage forms for oral administration |
-
2007
- 2007-08-22 CA CA002661616A patent/CA2661616A1/en not_active Abandoned
- 2007-08-22 WO PCT/EP2007/058696 patent/WO2008023027A2/en active Application Filing
- 2007-08-22 RU RU2009110253/15A patent/RU2009110253A/en not_active Application Discontinuation
- 2007-08-22 BR BRPI0715835-1A patent/BRPI0715835A2/en not_active IP Right Cessation
- 2007-08-22 MX MX2009001884A patent/MX2009001884A/en not_active Application Discontinuation
- 2007-08-22 EP EP07788511A patent/EP2056795A2/en not_active Withdrawn
- 2007-08-22 KR KR1020097006052A patent/KR20090045943A/en not_active Application Discontinuation
- 2007-08-22 AU AU2007287560A patent/AU2007287560A1/en not_active Abandoned
- 2007-08-22 JP JP2009525064A patent/JP2010501525A/en active Pending
- 2007-08-23 CL CL200702477A patent/CL2007002477A1/en unknown
- 2007-08-23 TW TW096131278A patent/TW200816998A/en unknown
- 2007-08-24 AR ARP070103757A patent/AR062509A1/en unknown
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2009
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WO2008023027A3 (en) | 2008-04-17 |
EP2056795A2 (en) | 2009-05-13 |
WO2008023027A2 (en) | 2008-02-28 |
BRPI0715835A2 (en) | 2013-07-23 |
AR062509A1 (en) | 2008-11-12 |
MX2009001884A (en) | 2009-03-06 |
CL2007002477A1 (en) | 2008-04-18 |
JP2010501525A (en) | 2010-01-21 |
KR20090045943A (en) | 2009-05-08 |
IL197130A0 (en) | 2009-11-18 |
RU2009110253A (en) | 2010-09-27 |
CA2661616A1 (en) | 2008-02-28 |
AU2007287560A1 (en) | 2008-02-28 |
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