JP2014162736A - Excipient agglomerated material, production method thereof, and tablet - Google Patents
Excipient agglomerated material, production method thereof, and tablet Download PDFInfo
- Publication number
- JP2014162736A JP2014162736A JP2013033265A JP2013033265A JP2014162736A JP 2014162736 A JP2014162736 A JP 2014162736A JP 2013033265 A JP2013033265 A JP 2013033265A JP 2013033265 A JP2013033265 A JP 2013033265A JP 2014162736 A JP2014162736 A JP 2014162736A
- Authority
- JP
- Japan
- Prior art keywords
- excipient
- sugar alcohol
- disaccharide
- granulated product
- 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.)
- Granted
Links
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Abstract
Description
本発明は、二糖類の糖アルコールを用いた賦形剤造粒物及びその製造方法、並びに錠剤に関する。 The present invention relates to an excipient granule using a disaccharide sugar alcohol, a method for producing the same, and a tablet.
従来、錠剤（錠菓を含む）などの賦形剤には糖や糖アルコールが使用されている。
前記糖としては、主として乳糖（例えば、特許文献１参照）や麦芽糖が価格や成形性の面で選択されるが、これらは還元糖と呼ばれるように分子中に還元基を有するため、錠剤に含まれる一部の成分とメイラード反応を起こすなど、安定性の面において問題を生じることがある。
一方、前記糖アルコールは分子中に還元基を有していないことから、錠剤に含まれる他成分との反応性が比較的低い点が評価されており、医薬分野ではＤ−マンニトールやソルビトール、食品分野ではマルチトールを主成分とした還元麦芽糖水飴やソルビトールなどが使用されている。
Conventionally, sugars and sugar alcohols have been used for excipients such as tablets (including tablet confectionery).
As the sugar, lactose (for example, see Patent Document 1) and maltose are selected in terms of price and moldability, and these are included in tablets because they have a reducing group in the molecule as called reducing sugar. This may cause problems in terms of stability, such as causing a Maillard reaction with some components.
On the other hand, since the sugar alcohol does not have a reducing group in the molecule, it has been evaluated for its relatively low reactivity with other components contained in tablets. In the pharmaceutical field, D-mannitol, sorbitol, food In the field, reduced maltose starch syrup and sorbitol, which are mainly composed of maltitol, are used.
錠剤の製造における打錠の際に高い錠剤硬度を得るためには、一次粒子の粒子径を細かくして比表面積を大きくする方法が考えられる。しかし、前記糖アルコールは、凝集性が強いため、一次粒子の粒子径が細かい場合には保管中に硬い凝集を発生することが多く、使用する際には解砕工程が必要となるという問題がある。
前記凝集を避けるため、原料メーカーでは粒度の大きい結晶品を扱うことが多いものの、これらはそのまま打錠しても十分な硬度を得ることができないという問題がある。そのため、いったん粉砕を行った後に造粒して使用するケースが多い。
このような結晶品を粉砕した微粉状の製品も原料メーカーにより供給されてはいるが、これらは輸送期間中に凝集が発生していることが多いため、使用する際には解砕工程が必要となるという問題は解消されていない。
In order to obtain high tablet hardness at the time of tableting in the production of tablets, a method of increasing the specific surface area by reducing the particle diameter of primary particles is conceivable. However, since the sugar alcohol has strong cohesiveness, when the primary particle size is small, hard aggregation often occurs during storage, and there is a problem that a crushing step is required when used. is there.
In order to avoid the agglomeration, raw material manufacturers often handle crystal products having a large particle size, but there is a problem in that sufficient hardness cannot be obtained even if they are tableted as they are. For this reason, there are many cases where granulation is performed after pulverization.
Although a fine powder product obtained by pulverizing such a crystal product is also supplied by the raw material manufacturer, agglomeration is often generated during the transportation period, so a crushing step is necessary when using it. The problem of becoming is not solved.
このような状況下、様々な糖アルコールの賦形剤の開発が行われており、例えば、単糖類の糖アルコール賦形剤としては、Ｄ−マンニトールではフロイント産業株式会社製「グラニュトール」、三菱商事フードテック株式会社製「マンニットＰ」、ロケット社「ＰＥＡＲＬＩＴＯＬ」、メルクミリポア社「Ｐｅｒｔｅｋ Ｍ」などが販売されており、ソルビトールでは物産フードサイエンス株式会社製「ソルビトールＦＰ」、ロケット社「ＮＥＯＳＯＲＢ」、メルクミリポア社「Ｐｅｒｔｅｋ ＳＩ」などが販売されている。単糖類のマンニトールやソルビトールについては錠剤用賦形剤としての利用も多く、直接打錠用に造粒された賦形剤のラインナップも豊富である。
しかし、マルチトール、イソマルト、ラクチトールといった二糖類の糖アルコールの直接打錠用賦形剤は単糖類のものに比べて少ない現状がある。
Under such circumstances, various sugar alcohol excipients have been developed. For example, as sugar alcohol excipients for monosaccharides, D-mannitol uses “Granitol” manufactured by Freund Sangyo Co., Ltd., Mitsubishi. “Mannit P” by Shoji Foodtech Co., Ltd., “PEARLITOL” by Rocket, “Pertek M” by Merck Millipore, etc. are sold. Sorbitol FP by Merchandise Food Science Co., Ltd. and NEOSORB by Rocket Merck Millipore "Pertek SI" and the like are sold. Monosaccharides such as mannitol and sorbitol are often used as excipients for tablets, and there is a wide lineup of excipients granulated for direct tableting.
However, excipients for direct tableting of disaccharide sugar alcohols such as maltitol, isomalt and lactitol are less present than those of monosaccharides.
二糖類の糖アルコールで市場に流通している製品としては、マルチトール、イソマルト、ラクチトールが挙げられる。これらのうちマルチトールについては、医薬品添加剤規格において還元麦芽糖水飴として掲載されており、マルチトールの精製度は８８．５％以上と定められている。そのため、国内で流通しているマルチトールの製品は約９０％〜９８％程度の低い精製度である還元麦芽糖水飴と９８％以上の高い精製度であるマルチトール結晶の２種類に分けることができる。
マルチトール精製度が低い還元麦芽糖水飴としては、例えば、三菱商事フードテック株式会社製「アマルティ」、「粉末マルチトールＧ−３」、上野製薬株式会社製「粉末マルチトールウエノ ６０Ｍ」が挙げられる。
また、精製度が高いマルチトール結晶品としては、例えば、三菱商事フードテック株式会社製「レシス」、カーギル社製「Ｍａｌｔｉｄｅｘ」、ロケット社製「ＳｗｅｅｔＰｅａｒｌ」が挙げられる。
Maltitol, isomalt, and lactitol are examples of products distributed in the market with disaccharide sugar alcohols. Of these, maltitol is listed as a reduced maltose starch syrup in the pharmaceutical additive standards, and the degree of purification of maltitol is defined as 88.5% or more. Therefore, maltitol products distributed in Japan can be divided into two types: reduced maltose starch syrup with a low purity of about 90% to 98% and maltitol crystals with a high purity of over 98%. .
Examples of the reduced maltose starch syrup having a low degree of maltitol purification include “Amarti”, “Powdered Maltitol G-3” manufactured by Mitsubishi Corporation Foodtech Co., Ltd., and “Powdered Maltitol Ueno 60M” manufactured by Ueno Pharmaceutical Co., Ltd.
Examples of the maltitol crystal product having a high degree of purification include “Resis” manufactured by Mitsubishi Corporation Foodtech, “Maltdex” manufactured by Cargill, and “SweetPearl” manufactured by Rocket.
これらに含まれるマルチトール以外の成分は、ソルビトールなどの副生成物である。この副生成物が多いと打錠時に高い錠剤硬度が得られやすいことから、打錠用賦形剤としては、精製度の低い還元麦芽糖水飴が選択されることが多い。直接打錠用賦形剤として、打錠に適した粒度に調製された製品は、還元麦芽糖水飴では、例えば、「アマルティ ＭＲ−５０」、「粉末マルチトールウエノ ６０Ｍ」などが存在する。
しかし、これらの製品は精製したのちに篩分けを行って粒度を調製したものが多く、粒子径が大きいことから流動性が高く、凝集性も比較的抑えられているものの更なる改良が求められており、また、一次粒子の形状としてはブロック状であり、打錠した際に粉砕品に比べて硬度が得られにくいものである。更に、製品中に含まれるソルビトールなどの副生成物には吸湿性があるために、水分に弱い成分との反応性に問題が残る。
Components other than maltitol contained in these are by-products such as sorbitol. When this by-product is large, a high tablet hardness is easily obtained at the time of tableting, and thus reduced maltose starch syrup is often selected as a tableting excipient. As a direct tableting excipient, products prepared in a particle size suitable for tableting include, for example, “Amarty MR-50”, “Powdered Maltitol Ueno 60M” and the like in reduced maltose starch syrup.
However, many of these products are refined and then subjected to sieving to prepare a particle size. Since the particle size is large, fluidity is high and cohesion is relatively suppressed, but further improvement is required. In addition, the primary particles have a block shape, and it is difficult to obtain hardness compared to the pulverized product when tableted. Furthermore, since by-products such as sorbitol contained in the product are hygroscopic, there remains a problem with reactivity with components that are sensitive to moisture.
また、マルチトールの精製度が高いマルチトール結晶品では、副生成物が少ないために成形性が低く、錠剤用賦形剤として用いられることは少なく、ガムやシロップなどに利用されることが多い。そのため市場に流通している製品は、粒度の大きい結晶品かそれの粉砕品が多く、直接打錠には適さない。 In addition, maltitol crystal products with a high degree of purification of maltitol have low by-products and thus have low moldability, are rarely used as excipients for tablets, and are often used for gums and syrups. . For this reason, the products on the market are mostly crystal products with a large particle size or pulverized products thereof, and are not suitable for direct tableting.
また、造粒された製品として、例えば、ロケット社「ＳｗｅｅｔＰｅａｒｌ Ｐ３００ＤＣ」が挙げられるが、体積平均粒子径が３００μｍ前後と通常の直接打錠用賦形剤に比べて大きいために、打錠しても高い成形性が得られず、有用な直接打錠用賦形剤とは言えない。 As a granulated product, for example, “SweetPearl P300DC” manufactured by Rocket Co., Ltd. is used. However, high moldability cannot be obtained, and it cannot be said that it is a useful excipient for direct tableting.
イソマルトとしては、例えば、カーギル社製「Ｉｓｏｍａｌｔｉｄｅｘ」、Ｂｅｎｅｏ−Ｐａｌａｔｉｎｉｔ社製「ＧａｌｅｎＩＱ」などが挙げられる。
また、ラクチトールとしては、三菱商事フードテック株式会社製「ミルヘン」、物産フードサイエンス株式会社製「ラクチトールＬＣ」などが挙げられる。
これらの製品も主にガムやチョコレートなどに使用される場合が多いため、粒度の大きい結晶品かそれの粉砕品が多く、直接打錠には適さない。
また、造粒された製品としては、例えば、Ｂｅｎｅｏ−Ｐａｌａｔｉｎｉｔ社「ＧａｌｅｎＩＱ ７１０」、「ＧａｌｅｎＩＱ ７２０」が挙げられるが、これらも通常の直接打錠用賦形剤に比べて体積平均粒子径が大きく設定されているために、高い成形性が得られない。
Examples of the isomalt include “Isomaltex” manufactured by Cargill and “GalenIQ” manufactured by Beneo-Palatinit.
Examples of lactitol include “Miruhen” manufactured by Mitsubishi Corporation Foodtech Co., Ltd. and “Lactitol LC” manufactured by Bussan Food Science Co., Ltd.
Since these products are often used mainly for gums and chocolates, there are many crystal products having a large particle size or pulverized products thereof, which are not suitable for direct tableting.
Examples of the granulated product include “GalenIQ 710” and “GalenIQ 720” by Beneo-Palatinit, which also have a larger volume average particle diameter than ordinary direct tableting excipients. Since it is set, high moldability cannot be obtained.
したがって、二糖類の糖アルコールを用い、長期間保管した場合であっても凝集を抑制することができ、成形性が高く、優れた錠剤硬度を得ることができ、更に、錠剤に含まれる成分との反応性が低い賦形剤造粒物はこれまで市場に流通しておらず、その開発が強く求められている。 Therefore, using a sugar sugar of a disaccharide, it is possible to suppress aggregation even when stored for a long period of time, high moldability, excellent tablet hardness can be obtained, and further, the ingredients contained in the tablet Granules of excipients with low reactivity have not been marketed so far, and their development is strongly demanded.
本発明は、従来における前記諸問題を解決し、以下の目的を達成することを課題とする。即ち、本発明は、長期間保管した場合であっても凝集を抑制することができ、成形性が高く、優れた錠剤硬度を得ることができ、更に、錠剤に含まれる成分との反応性が低い賦形剤造粒物及びその製造方法、並びに前記賦形剤造粒物を用いた錠剤を提供することを目的とする。 An object of the present invention is to solve the above-described problems and achieve the following objects. That is, the present invention can suppress agglomeration even when stored for a long period of time, has high moldability, can obtain excellent tablet hardness, and further has reactivity with components contained in the tablet. It is an object of the present invention to provide a low excipient granulated product, a method for producing the same, and a tablet using the excipient granulated product.
前記課題を解決するための手段としては、以下の通りである。即ち、
＜１＞ 二糖類の糖アルコールを含む粉体を流動層造粒装置内で流動させ、前記粉体に二糖類の糖アルコールを含有する液を噴霧して造粒することにより得られ、
前記造粒により得られる造粒物の体積平均粒子径が７０μｍ〜１７０μｍであり、
前記造粒物を、４０℃、相対湿度７５％の環境下で２週間保管したときの凝集率が３０％以下であることを特徴とする賦形剤造粒物である。
＜２＞ 粉体における二糖類の糖アルコールの体積平均粒子径が、５０μｍ以下である前記＜１＞に記載の賦形剤造粒物である。
＜３＞ 二糖類の糖アルコールを含有する液における二糖類の糖アルコールの含有量が、３０質量％以上である前記＜１＞から＜２＞のいずれかに記載の賦形剤造粒物である。
＜４＞ 二糖類の糖アルコールを含有する液における二糖類の糖アルコールの含有量が、５０質量％以上である前記＜１＞から＜３＞のいずれかに記載の賦形剤造粒物である。
＜５＞ 二糖類の糖アルコールが、マルチトール及び／又はイソマルトである前記＜１＞から＜４＞のいずれかに記載の賦形剤造粒物である。
＜６＞ 直接打錠用である前記＜１＞から＜５＞のいずれかに記載の賦形剤造粒物である。
＜７＞ 食品用である前記＜１＞から＜６＞のいずれかに記載の賦形剤造粒物である。
＜８＞ 医薬品用である前記＜１＞から＜６＞のいずれかに記載の賦形剤造粒物である。
＜９＞ 二糖類の糖アルコールを含む粉体を流動層造粒装置内で流動させ、前記粉体に二糖類の糖アルコールを含有する液を噴霧して造粒することにより得られ、
前記造粒により得られる造粒物の体積平均粒子径が７０μｍ〜１７０μｍであり、
前記造粒物を、４０℃、相対湿度７５％の環境下で２週間保管したときの凝集率が３０％以下であることを特徴とする賦形剤造粒物の製造方法である。
＜１０＞ 前記＜１＞から＜８＞のいずれかに記載の賦形剤造粒物と、食品素材又は活性成分とを含むことを特徴とする錠剤である。
＜１１＞ 直接打錠により得られる前記＜１０＞に記載の錠剤である。
Means for solving the problems are as follows. That is,
<1> obtained by allowing a powder containing a disaccharide sugar alcohol to flow in a fluidized bed granulator, spraying the powder containing a disaccharide sugar alcohol, and granulating the powder.
The volume average particle diameter of the granulated product obtained by the granulation is 70 μm to 170 μm,
An agglomerate having an agglomeration rate of 30% or less when the granulated product is stored for 2 weeks in an environment of 40 ° C. and 75% relative humidity.
<2> The excipient granule according to <1>, wherein the volume average particle diameter of the sugar sugar of the disaccharide in the powder is 50 μm or less.
<3> The excipient granule according to any one of <1> to <2>, wherein the content of the sugar alcohol of the disaccharide in the liquid containing the sugar alcohol of the disaccharide is 30% by mass or more. is there.
<4> The excipient granule according to any one of <1> to <3>, wherein the content of the disaccharide sugar alcohol in the liquid containing the disaccharide sugar alcohol is 50% by mass or more. is there.
<5> The excipient granule according to any one of <1> to <4>, wherein the sugar alcohol of the disaccharide is maltitol and / or isomalt.
<6> The excipient granule according to any one of <1> to <5>, which is used for direct tableting.
<7> The excipient granule according to any one of <1> to <6>, which is for food.
<8> The excipient granule according to any one of <1> to <6>, which is used for pharmaceuticals.
<9> A powder containing a sugar sugar of a disaccharide is fluidized in a fluidized bed granulator, and obtained by spraying and granulating a liquid containing the sugar alcohol of a disaccharide on the powder,
The volume average particle diameter of the granulated product obtained by the granulation is 70 μm to 170 μm,
A method for producing an excipient granulated product, wherein the granulated product has an aggregation rate of 30% or less when stored for 2 weeks in an environment of 40 ° C. and a relative humidity of 75%.
<10> A tablet comprising the excipient granulated product according to any one of <1> to <8> and a food material or an active ingredient.
<11> The tablet according to <10>, obtained by direct tableting.
本発明によれば、従来における前記諸問題を解決し、前記目的を達成することができ、長期間保管した場合であっても凝集を抑制することができ、成形性が高く、優れた錠剤硬度を得ることができ、更に、錠剤に含まれる成分との反応性が低い賦形剤造粒物及びその製造方法、並びに前記賦形剤造粒物を用いた錠剤を提供することができる。 According to the present invention, the conventional problems can be solved, the object can be achieved, aggregation can be suppressed even when stored for a long period of time, high moldability, and excellent tablet hardness. Furthermore, an excipient granulated product having a low reactivity with the components contained in the tablet, a method for producing the same, and a tablet using the excipient granulated product can be provided.
（賦形剤造粒物及びその製造方法）
本発明の賦形剤造粒物は、二糖類の糖アルコールを含む。
本発明の賦形剤造粒物は、本発明の賦形剤造粒物の製造方法により、好適に製造することができる。
以下、本発明の賦形剤造粒物の製造方法の説明と併せて、本発明の賦形剤造粒物についても説明する。
(Excipient granules and production method thereof)
The excipient granulated product of the present invention contains a sugar alcohol of a disaccharide.
The excipient granulated product of the present invention can be suitably produced by the method for producing an excipient granulated product of the present invention.
Hereinafter, the excipient granulated product of the present invention will be described together with the description of the method for producing the excipient granulated product of the present invention.
＜賦形剤造粒物の製造方法＞
本発明の賦形剤造粒物の製造方法は、二糖類の糖アルコールを含む粉体を流動層造粒装置内で流動させ、前記粉体に二糖類の糖アルコールを含有する液を噴霧して造粒する工程（以下、「造粒工程」と称することがある）を含み、必要に応じて更にその他の工程を含む。
<Method for producing excipient granulated product>
In the method for producing an excipient granulated product of the present invention, a powder containing a disaccharide sugar alcohol is flowed in a fluidized bed granulating apparatus, and a liquid containing the disaccharide sugar alcohol is sprayed on the powder. And a granulating step (hereinafter sometimes referred to as a “granulating step”), and further includes other steps as necessary.
＜＜造粒工程＞＞
前記造粒工程は、二糖類の糖アルコールを含む粉体を流動層造粒装置内で流動させ、前記粉体に二糖類の糖アルコールを含有する液を噴霧して造粒する工程であり、前記造粒により得られる造粒物の体積平均粒子径が７０μｍ〜１７０μｍである。
<< Granulation process >>
The granulation step is a step of causing a powder containing a disaccharide sugar alcohol to flow in a fluidized bed granulation apparatus, and spraying a liquid containing the disaccharide sugar alcohol on the powder to granulate. The granulated product obtained by the granulation has a volume average particle diameter of 70 μm to 170 μm.
−流動層造粒装置−
前記流動層造粒装置は、流動化（浮遊流動）された前記粉体に前記二糖類の糖アルコールを含有する液を噴霧し、前記粉体を前記二糖類の糖アルコールを含有する液によりコーティングし、前記粉体の粒子間に液体架橋の凝集を起こさせて造粒する装置である。
前記流動層造粒装置としては、特に制限はなく、公知の流動層造粒装置を適宜選択することができ、例えば、フローコーター、スパイラフロー、グラニュレックス（いずれも、フロイント産業株式会社製）などが挙げられる。
-Fluidized bed granulator-
The fluidized bed granulator sprays a liquid containing the disaccharide sugar alcohol onto the fluidized (floating fluid) powder, and coats the powder with a liquid containing the disaccharide sugar alcohol. Then, it is an apparatus for agglomerating liquid bridges between particles of the powder and granulating.
There is no restriction | limiting in particular as said fluidized-bed granulator, A well-known fluidized-bed granulator can be selected suitably, For example, a flow coater, Spiraflow, Granurex (all are the Freund Sangyo Co., Ltd. product) etc. Is mentioned.
−入口温度、風量−
前記流動の際の入口温度としては、特に制限はなく、目的に応じて適宜選択することができ、例えば、５０℃〜１００℃とすることができる。
前記流動の際の風量としては、特に制限はなく、目的に応じて適宜選択することができる。
−Inlet temperature, air volume−
There is no restriction | limiting in particular as inlet temperature in the case of the said flow, According to the objective, it can select suitably, For example, it can be set as 50 to 100 degreeC.
There is no restriction | limiting in particular as an air volume in the case of the said flow, According to the objective, it can select suitably.
−粉体−
前記粉体の態様としては、二糖類の糖アルコールを含んでいれば特に制限はなく、目的に応じて適宜選択することができるが、二糖類の糖アルコールのみからなる態様が好ましい。
-Powder-
The embodiment of the powder is not particularly limited as long as it contains a disaccharide sugar alcohol, and can be appropriately selected according to the purpose. However, an embodiment comprising only a disaccharide sugar alcohol is preferable.
−−二糖類の糖アルコール−−
前記二糖類の糖アルコールの体積平均粒子径としては、特に制限はなく、目的に応じて適宜選択することができるが、５０μｍ以下が好ましく、１０μｍ〜３０μｍがより好ましい。前記好ましい範囲であると、打錠した際に高い錠剤硬度が得られる点で、有利である。
前記体積平均粒子径は、公知の装置により測定することができ、例えば、レーザー回析／散乱式粒度分布測定装置（マイクロトラックＨＲＡ、日機装株式会社製）により測定することができる。
-Sugar alcohol of disaccharide-
There is no restriction | limiting in particular as a volume average particle diameter of the sugar alcohol of the said disaccharide, Although it can select suitably according to the objective, 50 micrometers or less are preferable and 10 micrometers-30 micrometers are more preferable. The preferable range is advantageous in that high tablet hardness is obtained when tableting.
The volume average particle diameter can be measured with a known apparatus, for example, with a laser diffraction / scattering type particle size distribution measuring apparatus (Microtrac HRA, manufactured by Nikkiso Co., Ltd.).
前記二糖類の糖アルコールとは、マルトース、ショ糖、スクロースなどの二糖類を還元して得られる糖アルコールである。
前記二糖類の糖アルコールは、還元の際に生じる副生成物を含んでいてもよい。
前記二糖類の糖アルコールの精製度としては、特に制限はなく、目的に応じて適宜選択することができるが、９６％以上が好ましい。前記精製度が低く、ソルビトールなどの副生成物が多いと、吸湿性が強くなり、水分に弱い活性成分との反応性が高まることがある。なお、イソマルトはＧＰＳとＧＰＭの２成分からなるが、この場合の精製度とはＧＰＳとＧＰＭの総含有量とする。
前記二糖類の糖アルコールとしては、特に制限はなく、目的に応じて適宜選択することができ、例えば、市場に流通しているものではマルチトール、イソマルト、ラクチトールなどが挙げられる。これらは、１種単独で使用してもよいし、２種以上を併用してもよい。これらの中でも、打錠した際に高い錠剤硬度が得られる点で、マルチトール、イソマルトが好ましい。
前記二糖類の糖アルコールの態様としては、例えば、結晶を粉砕して篩下し所望の粒子径としたものや、噴霧乾燥により得られるものなどが挙げられる。
前記二糖類の糖アルコールの調製方法としては、特に制限はなく、目的に応じて適宜選択することができ、例えば、粉末原料が大きい場合には粉砕し、体積平均粒子径を５０μｍ以下とする方法が挙げられる。
The disaccharide sugar alcohol is a sugar alcohol obtained by reducing disaccharides such as maltose, sucrose, and sucrose.
The sugar alcohol of the disaccharide may contain a by-product generated during the reduction.
There is no restriction | limiting in particular as the refinement | purification degree of the sugar alcohol of the said disaccharide, Although it can select suitably according to the objective, 96% or more is preferable. If the degree of purification is low and there are many by-products such as sorbitol, the hygroscopicity becomes strong and the reactivity with active ingredients that are weak against moisture may increase. In addition, although isomalt consists of two components of GPS and GPM, the refinement | purification degree in this case shall be the total content of GPS and GPM.
There is no restriction | limiting in particular as sugar alcohol of the said disaccharide, According to the objective, it can select suitably, For example, maltitol, isomalt, lactitol etc. are mentioned in what is distribute | circulating on the market. These may be used individually by 1 type and may use 2 or more types together. Among these, maltitol and isomalt are preferable in that high tablet hardness is obtained when tableting.
Examples of the sugar alcohol of the disaccharide include those obtained by crushing crystals and sieving to obtain a desired particle size, and those obtained by spray drying.
There is no restriction | limiting in particular as a preparation method of the sugar alcohol of the said disaccharide, According to the objective, it can select suitably, For example, when a powder raw material is large, it grind | pulverizes and the volume average particle diameter is 50 micrometers or less. Is mentioned.
−二糖類の糖アルコールを含有する液−
前記二糖類の糖アルコールを含有する液（以下、「結合液」と称することがある）の態様としては、二糖類の糖アルコールを含んでいれば特に制限はなく、目的に応じて適宜選択することができるが、二糖類の糖アルコールのみからなる態様が好ましい。
-Liquid containing sugar alcohol of disaccharide-
The aspect of the liquid containing the sugar alcohol of the disaccharide (hereinafter sometimes referred to as “binding liquid”) is not particularly limited as long as it contains the sugar alcohol of the disaccharide, and is appropriately selected according to the purpose. However, an embodiment consisting only of a disaccharide sugar alcohol is preferred.
−−二糖類の糖アルコール−−
前記結合液における前記二糖類の糖アルコールの含有量としては、特に制限はなく、目的に応じて適宜選択することができるが、３０質量％以上が好ましく、５０質量％以上がより好ましく、７０質量％以上が特に好ましい。前記結合液における前記二糖類の糖アルコールの含有量が３０質量％未満であると、造粒中にブロッキングが生じやすく、造粒することが困難となることがある。一方、前記好ましい範囲であると、実用的な液速度で造粒することが出来、短い時間での造粒が可能となる点で、有利である。
-Sugar alcohol of disaccharide-
There is no restriction | limiting in particular as content of the sugar alcohol of the said disaccharide in the said binding liquid, Although it can select suitably according to the objective, 30 mass% or more is preferable, 50 mass% or more is more preferable, 70 mass % Or more is particularly preferable. When the content of the sugar alcohol of the disaccharide in the binding liquid is less than 30% by mass, blocking may easily occur during granulation, and granulation may be difficult. On the other hand, the preferred range is advantageous in that it can be granulated at a practical liquid speed and can be granulated in a short time.
前記粉体における二糖類の糖アルコールの含有質量（Ａ）と、前記二糖類の糖アルコールを含有する液における二糖類の糖アルコールの含有質量（Ｂ）との比率としては、特に制限はなく、目的に応じて適宜選択することができるが、Ａ：Ｂが、８：２〜４：６が好ましい。前記好ましい範囲外であると、前記粉体における二糖類の糖アルコールの仕込み量が少なく造粒初期に正常な流動状態が得られにくくなったり、造粒時間が長くなったりすることがある。 The ratio of the sugar content (A) of the disaccharide sugar alcohol in the powder and the sugar content (B) of the disaccharide sugar alcohol in the liquid containing the disaccharide sugar alcohol is not particularly limited. Although it can select suitably according to the objective, 8: 2-4: 6 are preferable for A: B. If the amount is outside the preferred range, the amount of disaccharide sugar alcohol charged in the powder is small, and it may be difficult to obtain a normal fluid state in the initial stage of granulation, or the granulation time may be prolonged.
前記糖アルコールとしては、特に制限はなく、目的に応じて適宜選択することができ、例えば、前記粉体で記載したものと同様の糖アルコールが挙げられ、マルチトール、イソマルトが好適に挙げられる。前記糖アルコールは、１種単独で使用してもよいし、２種以上を併用してもよい。 There is no restriction | limiting in particular as said sugar alcohol, According to the objective, it can select suitably, For example, the sugar alcohol similar to what was described with the said powder is mentioned, Maltitol and isomalt are mentioned suitably. The said sugar alcohol may be used individually by 1 type, and may use 2 or more types together.
前記結合液に含有される溶媒としては、特に制限はなく、目的に応じて適宜選択することができるが、水が好ましい。前記結合液における水の含有量としては、特に制限はなく、目的に応じて適宜選択することができる。 There is no restriction | limiting in particular as a solvent contained in the said binding liquid, Although it can select suitably according to the objective, Water is preferable. There is no restriction | limiting in particular as content of the water in the said coupling | bonding liquid, According to the objective, it can select suitably.
前記結合液の調製方法としては、特に制限はなく、目的に応じて公知の方法に従って調製することができ、例えば、前記二糖類の糖アルコール、前記二糖類の糖アルコール以外の添加成分を水と混合し、攪拌等する方法などが挙げられる。 The method for preparing the binding solution is not particularly limited, and can be prepared according to a known method according to the purpose. For example, the disaccharide sugar alcohol and the disaccharide sugar alcohol are added with water and other added components. Examples of the method include mixing and stirring.
−噴霧−
前記結合液の前記粉体への噴霧の方法としては、特に制限はなく、目的に応じて適宜選択することができ、例えば、使用する流動層造粒装置に設けられた噴霧手段、例えば、スプレーガン、噴霧ノズルなどから噴霧する方法などが好適に挙げられる。
なお、このとき、前記噴霧の条件としては、特に制限はなく、公知の条件を採用することができ、目的に応じてその噴霧量、噴霧する霧粒子（ミスト）の大きさ、噴霧時間などを適宜選択することができる。前記噴霧にスプレーガン等を使用する場合、そのスプレー空気圧としては、例えば、０．１ＭＰａ〜０．５ＭＰａ程度が好ましい。
-Spray-
The method for spraying the binding liquid onto the powder is not particularly limited and may be appropriately selected depending on the intended purpose. For example, spray means provided in the fluidized bed granulator to be used, for example, spray The method of spraying from a gun, a spray nozzle, etc. is mentioned suitably.
At this time, the spraying conditions are not particularly limited, and publicly known conditions can be adopted. The spraying amount, the size of sprayed mist particles (mist), the spraying time, and the like are determined according to the purpose. It can be selected appropriately. When a spray gun or the like is used for spraying, the spray air pressure is preferably about 0.1 MPa to 0.5 MPa, for example.
−賦形剤造粒物−
以上の造粒工程により、本発明の体積平均粒子径が７０μｍ〜１７０μｍの賦形剤造粒物が得られる。
なお、必要に応じて造粒工程の後に、造粒物を５００μｍのふるいで篩過する工程を行ってもよい。
前記賦形剤造粒物の体積平均粒子径としては、７０μｍ〜１７０μｍであれば特に制限はなく、目的に応じて適宜選択することができるが、硬度が高く、体積平均粒子径の小さい食品素材又は活性成分との混合均一性が高まる点で、７０μｍ〜１００μｍが好ましく挙げられ、また、凝集性をより抑制することが可能な点では、１００μｍ〜１７０μｍが好ましく挙げられる。
前記体積平均粒子径は、上述と同様にして測定することができる。
-Excipient granules-
By the above granulation step, an excipient granulated product having a volume average particle diameter of 70 μm to 170 μm of the present invention is obtained.
In addition, you may perform the process of sieving a granulated material with a 500 micrometers sieve after a granulation process as needed.
The volume average particle diameter of the excipient granulated product is not particularly limited as long as it is 70 μm to 170 μm, and can be appropriately selected according to the purpose. However, the food material has high hardness and small volume average particle diameter. Or 70 micrometers-100 micrometers are mentioned preferably at the point which mixing uniformity with an active ingredient increases, and 100 micrometers-170 micrometers are mentioned preferably at the point which can suppress cohesion more.
The volume average particle diameter can be measured in the same manner as described above.
前記賦形剤造粒物を４０℃、相対湿度７５％の環境下で２週間保管したときの凝集率としては、３０％以下であれば特に制限はなく、目的に応じて適宜選択することができるが、２０％以下が好ましく、１０％以下がより好ましく、５％以下が特に好ましい。
本発明において、前記凝集率は、以下のようにして測定する。
前記賦形剤造粒物をポリエチレン袋に入れ、４０℃、相対湿度７５％の環境下で保管し、保管開始から２週間後に、賦形剤造粒物を目開き１．７ｍｍの篩でふるい、以下の式から算出する。
凝集率（％）＝（篩上に残った造粒物の質量／造粒物全体の質量）×１００
The agglomeration rate when the excipient granule is stored for 2 weeks in an environment of 40 ° C. and relative humidity of 75% is not particularly limited as long as it is 30% or less, and can be appropriately selected according to the purpose. However, it is preferably 20% or less, more preferably 10% or less, and particularly preferably 5% or less.
In the present invention, the aggregation rate is measured as follows.
The excipient granule is put in a polyethylene bag and stored in an environment of 40 ° C. and a relative humidity of 75%. After two weeks from the start of storage, the excipient granule is sieved with a sieve having an opening of 1.7 mm. Calculated from the following equation.
Aggregation rate (%) = (mass of the granulated material remaining on the sieve / mass of the entire granulated material) × 100
本発明の体積平均粒子径が７０μｍ〜１７０μｍである賦形剤造粒物は、長期間保管しても凝集が起きにくく、使用する際に、解砕作業が不要であり、取扱い性に優れる。また、前記賦形剤造粒物は、食品素材又は活性成分との反応性が低い。更に、比表面積が大きいために、高い錠剤硬度が得られ易く、成形性にも優れる。
そのため、本発明の賦形剤造粒物は、直接打錠用として、特に好適に用いることができ、食品用途、医薬品用途に好適に用いることができる。
The excipient granulated product having a volume average particle diameter of 70 μm to 170 μm of the present invention hardly aggregates even when stored for a long period of time, and does not require a crushing operation when used, and is excellent in handleability. The excipient granulated product has low reactivity with food materials or active ingredients. Furthermore, since the specific surface area is large, high tablet hardness is easily obtained and the moldability is excellent.
Therefore, the excipient granulated product of the present invention can be particularly suitably used for direct tableting, and can be suitably used for food applications and pharmaceutical applications.
（錠剤）
本発明の錠剤は、賦形剤造粒物と、食品素材又は活性成分とを含み、必要に応じて更にその他の成分を含む。
(tablet)
The tablet of this invention contains an excipient | filler granulated material, a foodstuff raw material, or an active ingredient, and also contains another component as needed.
＜賦形剤造粒物＞
前記賦形剤造粒物は、上述した本発明の賦形剤造粒物である。
前記錠剤における前記賦形剤造粒物の含有量としては、特に制限はなく、目的に応じて適宜選択することができ、例えば、２０質量％〜９９．９質量％が挙げられる。
<Excipient granules>
The excipient granulated product is the above-described excipient granulated product of the present invention.
There is no restriction | limiting in particular as content of the said excipient granulated material in the said tablet, According to the objective, it can select suitably, For example, 20 mass%-99.9 mass% are mentioned.
＜食品素材＞
前記食品素材としては、食品に用いることができれば特に制限はなく、目的に応じて適宜選択することができ、例えば、グルコサミン、アミノ酸、ビタミン類、コンドロイチン、ミネラル類、コラーゲン、ウコン、イチョウ葉、ブルーベリー、大豆イソフラボン、ローヤルゼリー、クロレラなどが挙げられる。
前記食品素材の体積平均粒子径としては、特に制限はなく、目的に応じて適宜選択することができる。
<Food ingredients>
The food material is not particularly limited as long as it can be used for food, and can be appropriately selected according to the purpose. For example, glucosamine, amino acids, vitamins, chondroitin, minerals, collagen, turmeric, ginkgo leaves, blueberries , Soy isoflavones, royal jelly, chlorella and the like.
There is no restriction | limiting in particular as a volume average particle diameter of the said foodstuff material, According to the objective, it can select suitably.
＜活性成分＞
前記活性成分としては、特に制限はなく、目的に応じて適宜選択することができ、例えば、高血圧薬、狭心薬、気管支拡張薬、向精神薬、抗不安薬、抗うつ薬、催眠鎮静薬、抗パーキンソン薬、アレルギー用薬、歯科口腔用薬、強心薬、解熱鎮痛消炎薬、抗ヒスタミン薬、鎮咳薬、制酸薬、生薬、降圧薬、抗生物質、抗菌剤、不整脈用薬、冠血管拡張薬、末梢血管拡張薬、高脂血症用薬、利胆薬、ホルモン薬、痛風治療薬、抗リウマチ薬、化学療法薬、糖尿病用薬、鎮吐薬、抗てんかん薬、交感神経興奮薬、骨粗鬆症用薬、抗悪性腫瘍薬、免疫抑制薬、泌尿器科用薬、胃腸薬、脳代謝改善薬、脳循環改善薬、呼吸促進薬、血管収縮薬、鎮暈薬、去痰薬、中枢神経作用用薬、潰瘍治療薬、胃粘膜修復薬、鎮痛鎮痙薬等に使用される活性成分などが挙げられ、具体的には、アセトアミノフェン、テモカプリル塩酸塩、カベルゴリン、ベシル酸アムロジピン、オメプラゾール、ランソプラゾール、ファモチジン、ラフチジン、エカベトナトリウム、クエン酸モサプリド、レバミピド、ボグリボース、リスペリドン、イミダプリル塩酸塩、メロキシカム、ミルナシプラン塩酸塩、レボフロキサシン、クラリスロマイシン、サルポグレラート塩酸塩、トスフロキサシントシル酸塩、タムスロシン塩酸塩、ミゾリビン、タクロリムス水和物、フルボキサミンマレイン酸塩、グリメピリド、ラモセトロン塩酸塩、ニコランジル、ドネペジル塩酸塩、酒石酸ゾルピデム、ピオグリタゾン塩酸塩、アレンドロン酸ナトリウム水和物、リセドロン酸ナトリウム水和物、アトルバスタチンカルシウム水和物、フルバスタチンナトリウム、ロラタジン、ロサルタンカリウム、パロキセチン塩酸塩水和物、ラベプラゾールナトリウム、リバビリン、コハク酸スマトリプタン、ペロスピロン塩酸塩水和物、フマル酸クエチアピン、オロパタジン塩酸塩、フェキソフェナジン塩酸塩、エバスチン、セフジトレンピボキシル、塩酸セフカペンピボキシル、バルサルタン、ビカルタミド、アカルボースなどが挙げられる。
前記活性成分の体積平均粒子径としては、特に制限はなく、目的に応じて適宜選択することができる。
<Active ingredient>
The active ingredient is not particularly limited and may be appropriately selected depending on the intended purpose. Examples thereof include hypertensive drugs, angina drugs, bronchodilators, psychotropic drugs, anxiolytic drugs, antidepressant drugs, and hypnotic sedative drugs. , Antiparkinson, allergy, dental, oral, cardiotonic, antipyretic analgesic, antihistamine, antitussive, antacid, herbal medicine, antihypertensive, antibiotic, antibacterial, arrhythmia, coronary Dilators, peripheral vasodilators, hyperlipidemic drugs, antibacterial drugs, hormonal drugs, gout drugs, antirheumatic drugs, chemotherapy drugs, antidiabetic drugs, antiemetics, antiepileptic drugs, sympathomimetic drugs, Osteoporosis drugs, antineoplastic drugs, immunosuppressive drugs, urological drugs, gastrointestinal drugs, cerebral metabolism improving drugs, cerebral circulation improving drugs, respiratory stimulants, vasoconstrictors, antipruritic drugs, expectorants, drugs for central nervous system action , Active ingredients used in ulcer treatment, gastric mucosal repair, analgesic and antispasmodics, etc. Specifically, acetaminophen, temocapryl hydrochloride, cabergoline, amlodipine besylate, omeprazole, lansoprazole, famotidine, lafutidine, ecabet sodium, mosapride citrate, rebamipide, voglibose, risperidone, imidapril hydrochloride, meloxicam, Milnacipran hydrochloride, levofloxacin, clarithromycin, sarpogrelate hydrochloride, tosufloxacin tosylate, tamsulosin hydrochloride, mizoribine, tacrolimus hydrate, fluvoxamine maleate, glimepiride, ramosetron hydrochloride, nicorandil, donepezil hydrochloride, tartaric acid Zolpidem, pioglitazone hydrochloride, alendronate sodium hydrate, risedronate sodium hydrate, atorvastatin calcium hydrate Fluvastatin sodium, loratadine, losartan potassium, paroxetine hydrochloride hydrate, rabeprazole sodium, ribavirin, sumatriptan succinate, perospirone hydrochloride hydrate, quetiapine fumarate, olopatadine hydrochloride, fexofenadine hydrochloride, ebastine, cefditoren Pivoxil, cefcapene hydrochloride pivoxil, valsartan, bicalutamide, acarbose and the like.
There is no restriction | limiting in particular as a volume average particle diameter of the said active ingredient, According to the objective, it can select suitably.
＜その他の成分＞
前記その他の成分としては、特に制限はなく、目的に応じて適宜選択することができ、例えば、滑沢剤、結合剤、流動化剤、甘味剤、吸湿剤、除湿剤、コーティング剤、色素、矯味矯臭剤、溶解補助剤などが挙げられる。これらは１種単独で使用してもよく、２種以上を併用してもよい。
<Other ingredients>
The other components are not particularly limited and may be appropriately selected depending on the purpose. For example, lubricants, binders, fluidizers, sweeteners, hygroscopic agents, dehumidifiers, coating agents, dyes, Examples include flavoring agents and solubilizing agents. These may be used alone or in combination of two or more.
前記滑沢剤としては、特に制限はなく、目的に応じて適宜選択することができ、例えば、ステアリン酸マグネシウム、ステアリン酸、ステアリン酸カルシウム、タルク、硬化油などが挙げられる。 The lubricant is not particularly limited and may be appropriately selected depending on the intended purpose. Examples thereof include magnesium stearate, stearic acid, calcium stearate, talc, and hardened oil.
前記結合剤としては、特に制限はなく、目的に応じて適宜選択することができ、例えば、結晶セルロースなどが挙げられる。 There is no restriction | limiting in particular as said binder, According to the objective, it can select suitably, For example, crystalline cellulose etc. are mentioned.
前記流動化剤としては、特に制限はなく、目的に応じて適宜選択することができ、例えば、親水性シリカ、疎水性シリカ、ケイ酸カルシウム、アルキルホスフェイト（ＰＡＰ）、水溶性高分子化合物、無水リン酸水素カルシウム、ケイ酸マグネシウム、ケイ酸カルシウム、軽質無水ケイ酸、含水二酸化ケイ素、酸化マグネシウムなどが挙げられる。 The fluidizing agent is not particularly limited and may be appropriately selected depending on the intended purpose. For example, hydrophilic silica, hydrophobic silica, calcium silicate, alkyl phosphate (PAP), water-soluble polymer compound, Anhydrous calcium hydrogen phosphate, magnesium silicate, calcium silicate, light anhydrous silicic acid, hydrous silicon dioxide, magnesium oxide and the like can be mentioned.
前記甘味剤としては、特に制限はなく、目的に応じて適宜選択することができ、例えば、アスパルテーム、グルコース、ガラクトース、マンノース、リボース、アラビノース、マルトース、ラクトース、イソマルトース、セロビオース、ゲンチオビオース、パラチノースなどが挙げられる。 The sweetener is not particularly limited and may be appropriately selected depending on the intended purpose.For example, aspartame, glucose, galactose, mannose, ribose, arabinose, maltose, lactose, isomaltose, cellobiose, gentiobiose, palatinose Can be mentioned.
＜錠剤の製造方法＞
前記錠剤の製造方法としては、特に制限はなく、目的に応じて適宜選択することができるが、直接打錠法が好適に挙げられる。この際、使用する混合機や打錠機などは一般的に用いられるものを使用することができる。
<Tablet production method>
There is no restriction | limiting in particular as a manufacturing method of the said tablet, Although it can select suitably according to the objective, The direct tableting method is mentioned suitably. At this time, generally used mixers and tableting machines can be used.
以下、本発明の実施例を説明するが、本発明は、これらの実施例に何ら限定されるものではない。 Examples of the present invention will be described below, but the present invention is not limited to these examples.
（実施例１）
＜賦形剤造粒物１＞
体積平均粒子径が１２μｍの還元麦芽糖水飴（マルチトールの精製度：９６．３％）の粉末を１，６００ｇ秤量し、流動層造粒装置（商品名：フローコーター、フロイント産業株式会社製）に仕込み、還元麦芽糖水飴（マルチトールの精製度：９６．３％）８０質量％水溶液１，０００ｇを噴霧し造粒した。
得られた造粒物を５００μｍのふるいで篩過し、体積平均粒子径が１２８μｍである賦形剤造粒物１を得た。
なお、前記賦形剤造粒物１の体積平均粒子径は、レーザー回析／散乱式粒度分布測定装置（マイクロトラックＨＲＡ、日機装株式会社製）を用いて測定した。
Example 1
<Excipient granulated product 1>
Weigh 1,600 g of reduced maltose starch syrup (volumetric purity: 96.3%) with a volume average particle size of 12 μm and place it in a fluidized bed granulator (trade name: Flow coater, manufactured by Freund Sangyo Co., Ltd.). Charged and granulated by spraying 1,000 g of 80% by weight aqueous solution of reduced maltose starch syrup (degree of purification of maltitol: 96.3%).
The obtained granulated product was sieved with a 500 μm sieve to obtain excipient granulated product 1 having a volume average particle size of 128 μm.
In addition, the volume average particle diameter of the excipient granulated product 1 was measured using a laser diffraction / scattering type particle size distribution measuring apparatus (Microtrac HRA, manufactured by Nikkiso Co., Ltd.).
＜凝集試験＞
前記賦形剤造粒物１をポリエチレン袋に入れ、４０℃、相対湿度７５％の環境下で保管した。保管開始から２週間後に測定した凝集率の結果を表１に示した。
なお、前記凝集率は、前記保管後の賦形剤造粒物１を目開き１．７ｍｍの篩でふるい、以下の式から算出した。
凝集率（％）＝（篩上に残った造粒物の質量／造粒物全体の質量）×１００
また、比較として、アマルティＭＲ−１００、アマルティＭＲ−５０（いずれも三菱商事フードテック株式会社製）についても同様にして凝集試験を行った。結果を表１に示した。
<Aggregation test>
The excipient granulated product 1 was put in a polyethylene bag and stored in an environment of 40 ° C. and a relative humidity of 75%. Table 1 shows the results of the aggregation rate measured two weeks after the start of storage.
The agglomeration rate was calculated from the following formula by sieving the granule 1 after storage with a sieve having a mesh size of 1.7 mm.
Aggregation rate (%) = (mass of the granulated material remaining on the sieve / mass of the entire granulated material) × 100
For comparison, Amalty MR-100 and Amarti MR-50 (both manufactured by Mitsubishi Corporation Foodtech Co., Ltd.) were similarly subjected to an agglutination test. The results are shown in Table 1.
表１の結果から、本発明の賦形剤造粒物１では全く凝集が認められなかった。一方、粒度が細かいアマルティＭＲ−１００では硬い凝集が発生し、解砕が困難な状態であった。また、前記賦形剤造粒物１と同等の粒度を有するアマルティＭＲ−５０についてもある程度の凝集が認められた。 From the results in Table 1, no aggregation was observed in the excipient granulated product 1 of the present invention. On the other hand, in the Amalty MR-100 with a fine particle size, hard agglomeration occurred and it was difficult to disintegrate. In addition, a certain degree of aggregation was observed for Amarty MR-50 having a particle size equivalent to that of the excipient granulated product 1.
＜錠剤１及び２＞
前記賦形剤造粒物１又はアマルティＭＲ−５０を用いてグルコサミン含有錠剤を調製し、得られた錠剤１及び２の硬度を錠剤硬度計（フロイント産業株式会社製）にて測定した。
なお、処方を表２に、混合条件及び打錠条件を表３に、錠剤硬度を表４に示した。
<Tablets 1 and 2>
Glucosamine-containing tablets were prepared using the excipient granulated product 1 or Amarty MR-50, and the hardness of the obtained tablets 1 and 2 was measured with a tablet hardness meter (manufactured by Freund Sangyo Co., Ltd.).
The formulation is shown in Table 2, the mixing conditions and tableting conditions are shown in Table 3, and the tablet hardness is shown in Table 4.
表４の結果から、本発明の賦形剤造粒物１を使用した錠剤１は、アマルティＭＲ−５０を用いた錠剤２に比べて優れた成形性を示した。
図１に、造粒物１及びアマルティＭＲ−５０の走査型電子顕微鏡（ＳＥＭ）写真を示した。アマルティＭＲ−５０は篩分けで粒度を調製しているため、賦形剤造粒物１に比べて一次粒子が大きく、比表面積が小さいために高い錠剤硬度が得られないと考えられる。
From the results of Table 4, tablet 1 using the excipient granulated product 1 of the present invention showed excellent moldability as compared to tablet 2 using Amalty MR-50.
In FIG. 1, the scanning electron microscope (SEM) photograph of the granulated material 1 and Amarty MR-50 was shown. Since Amarty MR-50 has a particle size adjusted by sieving, the primary particles are larger than the excipient granulated product 1 and the specific surface area is small, so it is considered that high tablet hardness cannot be obtained.
（実施例２）
＜賦形剤造粒物２＞
体積平均粒子径が２２８μｍのマルチトール結晶品（マルチトールの精製度：９９．５％）をダルトン社製の粉砕機（商品名：アトマイザー）にて粉砕し、体積平均粒子径が１５μｍのマルチトール粉砕品を得た。
前記マルチトール粉砕品を１，６００ｇ秤量し、流動層造粒装置（商品名：フローコーター、フロイント産業株式会社製）に仕込み、（マルチトールの精製度：９９．５％）８０質量％水溶液３，０００ｇを噴霧し造粒した。
得られた造粒物を５００μｍのふるいで篩過し、体積平均粒子径が１０９μｍである賦形剤造粒物２を得た。
なお、前記賦形剤造粒物２の体積平均粒子径は、実施例１と同様にして測定した。
(Example 2)
<Excipient granulated product 2>
A maltitol crystal product having a volume average particle size of 228 μm (purification degree of maltitol: 99.5%) is pulverized by a pulverizer (trade name: atomizer) manufactured by Dalton, and maltitol having a volume average particle size of 15 μm. A pulverized product was obtained.
1,600 g of the maltitol pulverized product was weighed and charged into a fluidized bed granulator (trade name: Flow Coater, manufactured by Freund Sangyo Co., Ltd.), and the 80% by weight aqueous solution 3 (purity of maltitol: 99.5%) , 000 g was sprayed and granulated.
The obtained granulated product was sieved with a 500 μm sieve to obtain excipient granulated product 2 having a volume average particle diameter of 109 μm.
The volume average particle diameter of the excipient granulated product 2 was measured in the same manner as in Example 1.
＜凝集試験＞
前記賦形剤造粒物２、及び前記マルチトール粉砕品（体積平均粒子径 １５μｍ）について、実施例１と同様にして凝集試験を行った。結果を表５に示した。
<Aggregation test>
For the excipient granulated product 2 and the maltitol pulverized product (volume average particle size 15 μm), an aggregation test was conducted in the same manner as in Example 1. The results are shown in Table 5.
表５の結果から、本発明の賦形剤造粒物２は、わずかに凝集があるものの、簡単に崩れる状態であった。一方、粒度が細かいマルチトール粉砕品では硬い凝集が発生し、解砕が困難な状態であった。 From the results shown in Table 5, the excipient granulated product 2 of the present invention was in a state of easily collapsing although there was slight aggregation. On the other hand, in the maltitol pulverized product having a fine particle size, hard agglomeration occurred and it was difficult to disintegrate.
＜錠剤３及び４＞
前記賦形剤造粒物２を用いてプラセボ錠を調製し、得られた錠剤の硬度を実施例１と同様にして測定した。
また、比較として、ＳｗｅｅｔＰｅａｒｌ Ｐ３００ＤＣ（ロケット社製）を用い、同様にプラセボ錠を調製し、得られた錠剤の硬度を実施例１と同様にして測定した。
なお、処方を表６に、混合条件及び打錠条件を表７に、錠剤硬度を表８に示した。
<Tablets 3 and 4>
A placebo tablet was prepared using the excipient granulated product 2, and the hardness of the obtained tablet was measured in the same manner as in Example 1.
As a comparison, a placebo tablet was similarly prepared using SweetPearl P300DC (manufactured by Rocket), and the hardness of the obtained tablet was measured in the same manner as in Example 1.
The formulation is shown in Table 6, the mixing conditions and tableting conditions are shown in Table 7, and the tablet hardness is shown in Table 8.
表８の結果から、本発明の賦形剤造粒物２を使用した錠剤３は、ＳｗｅｅｔＰｅａｒｌ Ｐ３００ＤＣを用いた錠剤４に比べて優れた成形性を示した。 From the results of Table 8, the tablet 3 using the excipient granulated product 2 of the present invention showed excellent moldability as compared with the tablet 4 using SweetPearl P300DC.
（比較例１）
体積平均粒子径が２２８μｍのマルチトール結晶品（マルチトールの精製度：９９．５％）をダルトン社製の粉砕機（商品名：アトマイザー）にて粉砕し、体積平均粒子径が１５μｍのマルチトール粉砕品を得た。
前記マルチトール粉砕品を１，６００ｇ秤量し、流動層造粒装置（商品名：フローコーター、フロイント産業株式会社製）に仕込み、マルチトール（マルチトールの精製度：９９．５％）２０質量％水溶液を噴霧し造粒した。しかし、造粒中に粉体がブロッキングを起こしたため、造粒物が得られなかった。
(Comparative Example 1)
A maltitol crystal product having a volume average particle size of 228 μm (purification degree of maltitol: 99.5%) is pulverized by a pulverizer (trade name: atomizer) manufactured by Dalton, and maltitol having a volume average particle size of 15 μm. A pulverized product was obtained.
1,600 g of the pulverized maltitol was weighed and charged into a fluidized bed granulator (trade name: Flow Coater, manufactured by Freund Corporation), maltitol (purification degree of maltitol: 99.5%) 20% by mass The aqueous solution was sprayed and granulated. However, since the powder caused blocking during granulation, a granulated product could not be obtained.
（実施例３）
＜賦形剤造粒物３＞
体積平均粒子径が６４８μｍのイソマルト（イソマルトの精製度：９９．４％）をダルトン社製の粉砕機（商品名：アトマイザー）にて粉砕し、体積平均粒子径が２１μｍのイソマルト粉砕品を得た。
前記イソマルト粉砕品を１，６００ｇ秤量し、流動層造粒装置（商品名：フローコーター、フロイント産業株式会社製）に仕込み、イソマルト（イソマルトの精製度：９９．４％）８０質量％水溶液１，０００ｇを噴霧し造粒した。
得られた造粒物を５００μｍのふるいで篩過し、体積平均粒子径が１２０μｍである賦形剤造粒物３を得た。
なお、前記賦形剤造粒物３の体積平均粒子径は、実施例１と同様にして測定した。
(Example 3)
<Excipient granulated product 3>
Isomalt with a volume average particle size of 648 μm (Isomalt purification: 99.4%) was pulverized with a pulverizer (trade name: atomizer) manufactured by Dalton Co. to obtain an isomalt pulverized product with a volume average particle size of 21 μm. .
1,600 g of the isomalt pulverized product was weighed and charged into a fluidized bed granulator (trade name: Flow coater, manufactured by Freund Sangyo Co., Ltd.) and isomalt (purity of isomalt: 99.4%) 80% by weight aqueous solution 1, 000 g was sprayed and granulated.
The obtained granulated product was sieved with a 500 μm sieve to obtain excipient granulated product 3 having a volume average particle size of 120 μm.
The volume average particle size of the excipient granulated product 3 was measured in the same manner as in Example 1.
＜凝集試験＞
前記賦形剤造粒物３、及び前記イソマルト粉砕品（体積平均粒子径 ２１μｍ）について、実施例１と同様にして凝集試験を行った。結果を表９に示した。
<Aggregation test>
For the excipient granulated product 3 and the isomalt pulverized product (volume average particle diameter of 21 μm), an aggregation test was conducted in the same manner as in Example 1. The results are shown in Table 9.
表９の結果から、本発明の賦形剤造粒物３には、ほとんど凝集は認められなかった。一方、粒度が細かいイソマルト粉砕品では硬い凝集が発生し、解砕が困難な状態であった。 From the results in Table 9, almost no aggregation was observed in the excipient granulated product 3 of the present invention. On the other hand, in the isomalt pulverized product with a fine particle size, hard agglomeration occurred and it was difficult to disintegrate.
＜錠剤５から７＞
前記賦形剤造粒物３を用いてプラセボ錠を調製し、得られた錠剤の硬度を実施例１と同様にして測定した。
また、比較として、ＧａｌｅｎＩＱ ７２０（Ｂｅｎｅｏ−Ｐａｌａｔｉｎｉｔ社製）及びＧａｌｅｎＩＱ ７２１（Ｂｅｎｅｏ−Ｐａｌａｔｉｎｉｔ社製）を用い、同様にプラセボ錠を調製し、得られた錠剤の硬度を実施例１と同様にして測定した。
なお、処方を表１０に、混合条件及び打錠条件を表１１に、錠剤硬度を表１２に示した。
<Tablets 5 to 7>
A placebo tablet was prepared using the excipient granulated product 3, and the hardness of the obtained tablet was measured in the same manner as in Example 1.
For comparison, GalenIQ 720 (Beneo-Palatinit) and GalenIQ 721 (Beneo-Palatinit) were similarly used to prepare placebo tablets, and the hardness of the tablets obtained was measured in the same manner as in Example 1. did.
The formulation is shown in Table 10, the mixing conditions and tableting conditions are shown in Table 11, and the tablet hardness is shown in Table 12.
表１２の結果から、本発明の賦形剤造粒物３を使用した錠剤５は、ＧａｌｅｎＩＱ ７２０又は７２１を用いた錠剤６及び７に比べて優れた成形性を示した。 From the results of Table 12, the tablet 5 using the excipient granulated product 3 of the present invention showed excellent moldability as compared with the tablets 6 and 7 using GalenIQ 720 or 721.
（比較例２）
体積平均粒子径が６４８μｍのイソマルト（イソマルトの精製度：９９．４％）をダルトン社製の粉砕機（商品名：アトマイザー）にて粉砕し、体積平均粒子径が２１μｍのイソマルト粉砕品を得た。
前記イソマルト粉砕品を１，６００ｇ秤量し、流動層造粒装置（商品名：フローコーター、フロイント産業株式会社製）に仕込み、イソマルト（イソマルトの精製度：９９．４％）２５質量％水溶液を噴霧し造粒した。しかし、造粒中に粉体がブロッキングを起こしたため、造粒物が得られなかった。
(Comparative Example 2)
Isomalt with a volume average particle size of 648 μm (Isomalt purification: 99.4%) was pulverized with a pulverizer (trade name: atomizer) manufactured by Dalton Co. to obtain an isomalt pulverized product with a volume average particle size of 21 μm. .
1,600 g of the isomalt pulverized product was weighed and charged into a fluidized bed granulator (trade name: Flow coater, manufactured by Freund Sangyo Co., Ltd.) and sprayed with a 25% by weight aqueous solution of isomalt (purity of isomalt: 99.4%). Then granulated. However, since the powder caused blocking during granulation, a granulated product could not be obtained.
（実施例４）
＜錠剤８から１０＞
前記賦形剤造粒物２及び３、並びにアマルティＭＲ−５０を用い、表１３に示す処方にてグルコサミン含有錠剤を調製した。なお、混合条件及び打錠条件を表１４に示した。
Example 4
<Tablets 8 to 10>
Glucosamine-containing tablets were prepared with the formulation shown in Table 13 using the excipient granulated materials 2 and 3 and Amarty MR-50. The mixing conditions and tableting conditions are shown in Table 14.
＜保管試験＞
前記錠剤８から１０を密栓状態にて６０℃の環境下で２週間保管した。保管前後の錠剤の色差を色差計（商品名：ＳＺ−Σ９０、日本電色工業株式会社製）にて測定し、ΔＥの数値を比較した。結果を図２に示した
図２の結果から、本発明の賦形剤造粒物２又は３を使用した錠剤８及び９は、アマルティＭＲ−５０を用いた錠剤１０に比べて色の変化が抑えられており、グルコサミンとの反応性が低いことを確認された。
<Storage test>
The tablets 8 to 10 were stored in a sealed state in an environment at 60 ° C. for 2 weeks. The color difference between tablets before and after storage was measured with a color difference meter (trade name: SZ-Σ90, manufactured by Nippon Denshoku Industries Co., Ltd.), and the numerical value of ΔE was compared. The results are shown in FIG. 2. From the results of FIG. 2, the tablets 8 and 9 using the excipient granulated product 2 or 3 of the present invention have a color change compared to the tablet 10 using Amalty MR-50. It was confirmed that the reactivity with glucosamine was low.
本発明の賦形剤造粒物は、長期間保管した場合であっても凝集を抑制することができ、成形性が高く、優れた錠剤硬度を得ることができ、更に、錠剤に含まれる成分との反応性が低いので、錠剤の製造に用いることができ、特に、直接打錠用として好適に用いることができる。 The excipient granulated product of the present invention can suppress aggregation even when stored for a long period of time, has high moldability, can obtain excellent tablet hardness, and further contains ingredients contained in the tablet. Can be used for the production of tablets, and can be suitably used particularly for direct tableting.
Claims (7)
前記造粒により得られる造粒物の体積平均粒子径が７０μｍ〜１７０μｍであり、
前記造粒物を、４０℃、相対湿度７５％の環境下で２週間保管したときの凝集率が３０％以下であることを特徴とする賦形剤造粒物。 It is obtained by allowing powder containing disaccharide sugar alcohol to flow in a fluidized bed granulator, spraying the powder containing disaccharide sugar alcohol and granulating the powder,
The volume average particle diameter of the granulated product obtained by the granulation is 70 μm to 170 μm,
An excipient granulated product, wherein the granulated product has an agglomeration rate of 30% or less when stored for 2 weeks in an environment of 40 ° C. and a relative humidity of 75%.
前記造粒により得られる造粒物の体積平均粒子径が７０μｍ〜１７０μｍであり、
前記造粒物を、４０℃、相対湿度７５％の環境下で２週間保管したときの凝集率が３０％以下であることを特徴とする賦形剤造粒物の製造方法。 It is obtained by allowing powder containing disaccharide sugar alcohol to flow in a fluidized bed granulator, spraying the powder containing disaccharide sugar alcohol and granulating the powder,
The volume average particle diameter of the granulated product obtained by the granulation is 70 μm to 170 μm,
A method for producing an excipient granulated product, wherein the granulated product has an aggregation rate of 30% or less when stored for 2 weeks in an environment of 40 ° C and 75% relative humidity.
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| JP2006070046A (en) * | 1999-06-18 | 2006-03-16 | Takeda Chem Ind Ltd | Quick disintegrable solid preparation |
| JP2007509129A (en) * | 2003-10-21 | 2007-04-12 | カーギル インコーポレイテッド | Method for producing solid maltitol and its use in food and medicine |
| WO2009066644A1 (en) * | 2007-11-19 | 2009-05-28 | Freund Corporation | Spherical particle and method for producing the same |
| JP2009148262A (en) * | 2007-12-20 | 2009-07-09 | Roquette Freres | Granulated maltitol for direct compression and method of preparation thereof |
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| JP2016214107A (en) * | 2015-05-15 | 2016-12-22 | フロイント産業株式会社 | Production method of powder composition containing dead cell of lactic acid bacterium and/or bifidobacterium |
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