JP6426410B2 - Lyophilized formulation for storage at room temperature - Google Patents
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Description
本発明は、室温保存において安定な凍結乾燥製剤に関する。 The present invention relates to a lyophilized formulation that is stable at room temperature storage.
従来の注射用ハンプ製剤は、添加剤としてマンニトールを配合した凍結乾燥製剤である。この製剤は、安定性の観点から冷所保存が必要であり、医療現場からは、より取り扱いが簡便な、室温保存が可能な製剤が求められていた。室温保存を貯法とする製剤については、一定の温度変動の下での保存でも品質を保証するため、動的な準苛酷条件(40〜50℃下、1〜3ヶ月間保管)においても、可能な限り品質が保たれていることが必要とされる。 The conventional injectable hump preparation is a lyophilized preparation containing mannitol as an additive. This preparation needs to be stored in a cold place from the viewpoint of stability, and from the medical site, a preparation that can be stored at room temperature and that is easier to handle has been required. With regard to preparations that are stored at room temperature, it is possible even under dynamic quasi-hard conditions (storage at 40 to 50 ° C for 1 to 3 months) in order to guarantee the quality even when stored under constant temperature fluctuations. It is necessary that the quality be maintained as much as possible.
凍結乾燥製剤において、主薬(ペプチド、タンパク質)の化学的な保存安定性を改善する添加物としては、シュクロース(精製白糖)等の二糖類が知られている(特許文献1)が、この文献では、実験室レベルの少量を用いて、主薬の化学的安定性を評価しているのみであり、凍結乾燥製剤の品質の観点からも安定であるかは不明であった。特に、精製白糖は、代表的な安定化剤の一つであり、医薬品添加物としての使用実績量も多く製剤設計における使用量の自由度が高いといえる。しかしながら、凍結乾燥製剤の製造において乾燥対象物の量や濃度を高くすると、安定性やその他の製剤特性を含め、重要な品質が損なわれる危険性がある。 In freeze-dried preparations, disaccharides such as sucrose (purified sucrose) are known as additives for improving the chemical storage stability of the main drug (peptide, protein) (Patent Document 1). So, only small amounts at the laboratory level were used to evaluate the chemical stability of the main drug, and it was unclear whether it was stable from the viewpoint of the quality of the lyophilized preparation. In particular, refined sucrose is one of the typical stabilizers, and it can be said that the amount of use as a pharmaceutical additive is large and the degree of freedom of the amount used in formulation design is high. However, if the amount and concentration of the substance to be dried is increased in the preparation of the lyophilized formulation, there is a risk that important qualities may be lost, including stability and other formulation characteristics.
本発明は、精製白糖を主成分として一定量以上含み、室温保存において、主薬が化学的に安定であると共に、その他の製剤品質も安定な、生理活性ペプチドを有効成分として含有する凍結乾燥製剤を提供することを課題とする。 The present invention is a freeze-dried preparation containing a physiologically active peptide as an active ingredient, which comprises purified white sugar as a main ingredient and which contains a certain amount or more and which is stable at room temperature while the main drug is chemically stable and the quality of other preparations is also stable. The task is to provide.
カルペリチドの凍結乾燥製剤の再溶解液は、直接患者へ投与される可能性があるため、注射用水により等張が得られるように調製される必要がある。再溶解液量が少ない場合、薬液がバイアルに残留することによる投与保証量の低下の影響が大きくなるため、一定量以上の再溶解液を用いることが望ましく、精製白糖の量は当該液量で等張を得るため、一定量以上を使用する必要がある。 A reconstitution solution of a lyophilized formulation of carperitide needs to be prepared to be isotonic with water for injection, as it may be administered directly to the patient. If the amount of redissolved solution is small, the influence of the decrease in the dosage guarantee amount due to the remaining drug solution in the vial becomes large, so it is desirable to use a fixed amount or more of the redissolved solution. In order to obtain isotonicity, it is necessary to use a certain amount or more.
凍結乾燥製剤において、凍結乾燥体の外観形状と含有水分量は、製品の重要品質を確保する上で指標となる製剤特性である。外観形状が不良である凍結乾燥体は、再溶解時の溶解不良や溶解時間の長時間化等を引き起こす可能性があり、医療現場において問題が生じる可能性がある。また、凍結乾燥体の含有水分量が多い場合、凍結乾燥体としてのガラス転移温度を引き下げて、主薬の化学的安定性を損ねる原因、あるいは、保存中の凍結乾燥体の外観形状変化を促す原因となる可能性がある。 In the freeze-dried preparation, the appearance shape of the freeze-dried body and the water content are formulation characteristics that serve as an index for securing the important quality of the product. The lyophilizate having a poor appearance shape may cause dissolution failure at the time of re-dissolution, prolongation of the dissolution time, and the like, which may cause problems in the medical field. In addition, when the freeze-dried product contains a large amount of water, it lowers the glass transition temperature of the freeze-dried product to impair the chemical stability of the main drug or to promote the change in appearance of the freeze-dried product during storage. It could be
凍結乾燥体の外観形状を適切に確保するには、製造(真空凍結乾燥の工程中)及び凍結乾燥後の製品保管において凍結乾燥体が外観異常を来たさないことが必要となる。 In order to properly secure the appearance of the lyophilizate, it is necessary that the lyophilizate does not have an appearance abnormality in production (during the vacuum lyophilization step) and product storage after lyophilization.
製造工程(真空凍結乾燥)の途上において、凍結乾燥体に外観異常が生じる代表的な原因として、水蒸気による既乾燥部のコラプス(微小構造の融解様の崩壊)が挙げられる。また、製品保管における凍結乾燥体の外観変化の代表的な現象例として、暴露温度に対する凍結乾燥体の熱耐性の限界に起因するシュリンク(形状の縮み)等が挙げられる。 During the manufacturing process (vacuum lyophilization), as a typical cause of appearance abnormalities in the freeze-dried product, collapse of dried parts by steam (melting like collapse of microstructure) can be mentioned. In addition, as a typical phenomenon example of the appearance change of the freeze-dried product during product storage, there may be mentioned shrinkage (shrinkage of shape) due to the limit of the heat resistance of the freeze-dried product to the exposure temperature.
製造時のコラプスは、真空凍結乾燥工程の昇華過程において、既乾燥部における水蒸気の通過経路の狭窄または閉塞による水蒸気通過(昇華)の妨害、即ち、水分除去プロセスの異常により促進される。真空凍結乾燥工程においては、製剤容器に充填された凍結乾燥用液の上面から下面方向(深さ方向)へ向かって昇華が進行するため、真空凍結乾燥プロセスにおいて、コラプスは水分除去効率の低下要因になり、凍結乾燥体の水分量を高く推移させることとなる。即ち、製造段階で、既に異常な外観形状と高い水分量を有する凍結乾燥体が得られる場合があり、このとき、高い水分量は、製造段階における外観形状の変化の結果であると共に、凍結乾燥体のガラス転移温度を低下させ製剤保管中の化学的安定性の低下やシュリンクの原因にもなりうる。 Collapse during production is accelerated by the obstruction of water vapor passage (sublimation) due to the constriction or blockage of the water vapor passage path in the dried part, ie, an abnormality in the water removal process, in the sublimation process of the vacuum lyophilization process. In the vacuum lyophilization process, since sublimation proceeds from the upper surface to the lower surface direction (depth direction) of the lyophilization solution filled in the preparation container, in the vacuum lyophilization process, collapse causes a reduction in water removal efficiency. As a result, the water content of the freeze-dried product is kept high. That is, a lyophilizate having an abnormal appearance shape and a high water content may be obtained in the production stage, and at this time, a high water content is a result of changes in the appearance shape at the production stage and It can lower the glass transition temperature of the body and cause chemical stability and storage during storage.
製品保管時などの熱暴露によるシュリンクは、凍結乾燥体のガラス転移温度が、保管温度に対して適切に設計されていない場合に生じる可能性が高い。凍結乾燥体が暴露される温度が、凍結乾燥体に含まれる成分のガラス転移点を上回る場合、凍結乾燥体における化学反応速度が大きくなる、あるいは、凍結乾燥体の形状が変化するなどの確率が高くなる。例えば、主成分がシュクロースである凍結乾燥体の場合、凍結乾燥体が暴露される温度がシュクロースのガラス転移温度以下のとき、シュクロースは非晶質固体として存在するが、ガラス転移温度付近またはそれ以上の温度に暴露されたとき、相状態はゴム領域となる可能性が高くなる。こうした相変化が起こる場合、ペプチドなどの医薬活性成分を含有する凍結乾燥体においては、化学的反応速度が顕著に大きくなり、シュクロースによる活性成分の化学的な安定化効果は失われる。即ち、シュクロースの相変化は、上で述べた、凍結乾燥体の形状変化という物理的な特性変化の一因になると同時に、主薬の化学的安定化効果の低下原因にもなる。 Shrinkage due to thermal exposure, such as during product storage, is likely to occur when the glass transition temperature of the lyophilisate is not properly designed for the storage temperature. If the temperature to which the lyophilizate is exposed exceeds the glass transition temperature of the components contained in the lyophilizate, there is a probability that the chemical reaction rate in the lyophilizate increases, or the shape of the lyophilizate changes, etc. Get higher. For example, in the case of a lyophilizate in which the main component is sucrose, sucrose is present as an amorphous solid when the temperature to which the lyophilizate is exposed is below the glass transition temperature of sucrose, but near the glass transition temperature When exposed to temperatures above that, the phase state is likely to be a rubbery region. When such a phase change occurs, in a lyophilizate containing a pharmaceutically active ingredient such as a peptide, the chemical reaction rate is significantly increased, and the chemical stabilization effect of the active ingredient by sucrose is lost. That is, the phase change of sucrose not only contributes to the physical property change of the shape change of the lyophilizate described above, but also the decrease of the chemical stabilization effect of the main drug.
このように、精製白糖を一定量以上用いた凍結乾燥製剤において、製剤の品質を適切に維持できる製剤設計を行う必要があり、また、製剤設計においては、製剤品質の確保のため、外観形状や水分含量を指標とすることができる。 Thus, in a freeze-dried preparation using a certain amount or more of purified white sugar, it is necessary to design a preparation that can appropriately maintain the quality of the preparation. The water content can be used as an indicator.
本発明者等は、室温保存において安定な生理活性ペプチドの凍結乾燥製剤について鋭意検討した結果、内径22.1mmの円筒形ガラスバイアルを用いて、精製白糖の含有量を100〜1000mgで変動させた凍結乾燥製剤を作製し、製造時の特性評価や熱苛酷保管後の安定性試験を行った結果、精製白糖300〜500mg、溶解液の白糖濃度125mg/mL以下の製剤では良好な外観形状と水分含量を維持したこと、精製白糖が100mg又は1000mgの製剤では、製造時または熱苛酷試験において良好な外観形状と水分含量を保てなかったことを見出し、さらに検討を進めて本発明を完成するに至った。 As a result of intensive studies on a lyophilized preparation of a physiologically active peptide stable at room temperature storage, the present inventors varied the content of refined sucrose at 100 to 1000 mg using a cylindrical glass vial with an inner diameter of 22.1 mm. As a result of preparing a freeze-dried preparation and conducting the characteristic evaluation at the time of manufacture and the stability test after heat severe storage, good appearance shape and moisture are obtained for the preparation of refined sucrose 300 to 500 mg and formulation having sucrose concentration of 125 mg / mL or less. The content was maintained, and it was found that the preparation with 100 mg or 1000 mg of purified sucrose could not maintain a good appearance shape and water content in manufacturing or heat stress tests, and further studies were conducted to complete the present invention. It reached.
本発明は、以下を提供するものである。
(1) 有効量のペプチド性薬物、及び、容器の内部断面積に対して、約0.50〜1.85mg/mm2の精製白糖、を含有し、且つ、室温保存において安定であること、を特徴とする凍結乾燥製剤。
(2) 40℃、1ヶ月保管後において、凍結乾燥体が良好な外観形状を呈し、且つ、含有水分が1%以下であることを特徴とする、(1)の凍結乾燥製剤。
(3) 50℃、1ヶ月保管後において、凍結乾燥体が良好な外観形状を呈し、且つ、含有水分が1%以下であることを特徴とする、(1)の凍結乾燥製剤。
(4) 精製白糖の含有量が、容器の内部断面積に対して、約0.75〜1.35mg/mm2、である、(1)の凍結乾燥製剤。
(5) 容器が、内径が約20〜29 mmの円柱バイアルであり、精製白糖を約300〜500mg含有する、(1)の凍結乾燥製剤。
(6) 円柱バイアルの内径が約22.1 mmである(5)の凍結乾燥製剤。
(7) 精製白糖濃度が140mg/mL以下の溶解液を凍結乾燥することで製造された、(1)乃至(6)の何れかに記載の凍結乾燥製剤。
(8) ペプチド性薬物として、1mgのカルペリチドを含有する、(1)〜(7)の何れかに記載の凍結乾燥製剤。
(9) 固形成分として、実質的に精製白糖及びペプチド性薬物からなる(1)〜(8)の何れかに記載の凍結乾燥製剤。
(10) 精製白糖140mg/mL以下、及び、有効量のペプチド性薬物、を含有する水性溶液を、容器に、該容器の内部断面積に対して、約0.50〜1.85mg/mm2となるように充填し、当該充填された容器を凍結乾燥する工程を含む、室温保存において安定であること、を特徴とする凍結乾燥製剤の製造方法。
(11) 製造される凍結乾燥製剤において、良好な製剤品質特性を有する製剤の割合が約80%以上であることを特徴とする、(10)に記載の製造方法。
The present invention provides the following.
(1) containing an effective amount of a peptidic drug, and about 0.50 to 1.85 mg / mm 2 of purified sucrose with respect to the internal cross-sectional area of the container, and being stable at room temperature storage, A freeze-dried preparation characterized by
(2) The freeze-dried preparation according to (1), wherein the freeze-dried product has a good appearance after storage at 40 ° C. for one month, and the water content is 1% or less.
(3) The freeze-dried preparation according to (1), wherein the freeze-dried product has a good appearance after storage at 50 ° C. for one month, and the water content is 1% or less.
(4) The lyophilized formulation of (1), wherein the content of purified sucrose is about 0.75-1.35 mg / mm 2 with respect to the internal cross-sectional area of the container.
(5) The lyophilized formulation of (1), wherein the container is a cylindrical vial having an inner diameter of about 20 to 29 mm and contains about 300 to 500 mg of purified sucrose.
(6) A lyophilized formulation according to (5), wherein the inner diameter of the cylindrical vial is about 22.1 mm.
(7) The freeze-dried preparation according to any one of (1) to (6), which is produced by freeze-drying a solution having a purified sucrose concentration of 140 mg / mL or less.
(8) The lyophilized formulation according to any one of (1) to (7), which contains 1 mg of carperitide as a peptidic drug.
(9) The lyophilized formulation according to any one of (1) to (8), which substantially comprises purified sucrose and a peptidic drug as solid components.
(10) An aqueous solution containing 140 mg / mL or less of purified sucrose and an effective amount of a peptidic drug, in an amount of about 0.50 to 1.85 mg / mm 2 with respect to the internal cross-sectional area of the container. A method for producing a lyophilised preparation, characterized in that it is stable at room temperature storage, comprising the steps of: filling as such, and lyophilizing the filled container.
(11) The method according to (10), wherein the proportion of the preparation having good preparation quality characteristics is about 80% or more in the freeze-dried preparation to be manufactured.
本発明に係る凍結乾燥製剤は、室温保存において、有効成分の化学的安定性のみならず、凍結乾燥体の物理的安定性も確保されているため、流通、医療現場での保管場所として冷蔵庫等の設備を必要としないばかりでなく、使用に当っての薬剤の準備においても室温に戻すような手間も無く、更に注射溶液による再溶解時には、短時間で均一な溶液を得ることができる。 Since the freeze-dried preparation according to the present invention not only ensures the chemical stability of the active ingredient but also the physical stability of the freeze-dried product when stored at room temperature, it can be used as a storage location in distribution and medical fields Not only does it require the following equipment, but there is no need to bring it back to room temperature even when preparing a drug for use, and a uniform solution can be obtained in a short time when re-dissolving with an injection solution.
以下、本発明について詳細に説明する。 Hereinafter, the present invention will be described in detail.
本発明は、有効量のペプチド性薬物、及び、容器の内部断面積に対して、約0.50〜1.85mg/mm2の精製白糖、を含有し、且つ、室温保存において安定であること、を特徴とする凍結乾燥製剤を提供する。 The present invention contains an effective amount of a peptidic drug, and about 0.50 to 1.85 mg / mm 2 of purified sucrose with respect to the internal cross-sectional area of the container, and is stable at room temperature storage And a freeze-dried preparation characterized by
本発明において、「凍結乾燥製剤」とは、所定の組成からなる成分の溶液(「溶解液」という)を、容器に所定量注入し、真空凍結乾燥法により乾燥させた固形物(「凍結乾燥体」、又は、「凍結乾燥ケーキ」という)とそれを含む密閉の容器施栓系からなる製剤である。医療現場での使用時には、所定の水性成分を所定量容器に添加して、凍結乾燥体を溶解(「再溶解」という)して、溶液として対象へ投与される。 In the present invention, a "lyophilized preparation" refers to a solid (a "lyophilized" obtained by injecting a predetermined amount of a solution of components having a predetermined composition (referred to as a "lysate") into a container and drying by a vacuum freeze drying method. Or "a freeze-dried cake") and a closed container closure system containing it. At the time of use at a medical site, a predetermined aqueous component is added to a predetermined amount container, and the lyophilizate is dissolved (referred to as "re-dissolution") and administered to a subject as a solution.
本発明において「容器の内部断面積」とは、凍結乾燥に用いられる容器の胴ストレート部の水平方向の断面における内部断面積をいう。ここで、容器の胴ストレート部とは、容器下部の垂直方向の一定範囲において、水平方向の断面が均一な部分である。内部断面積とは、容器の水平方向の断面において、容器壁の内側の面積を意味する。 In the present invention, "the internal cross-sectional area of the container" refers to the internal cross-sectional area in the horizontal cross-section of the barrel straight portion of the container used for lyophilization. Here, the torso straight portion of the container is a portion having a uniform horizontal cross section in a predetermined range in the vertical direction of the lower portion of the container. The internal cross-sectional area means the area inside the container wall in the horizontal cross section of the container.
本発明において、「室温保存」とは、製剤の製造から使用までの期間、冷蔵庫、冷凍庫、保温庫などの温度調節設備を用いずに保存されることを意味する。このような室温保存が可能な医薬品は、その保存条件において、所定の期間安定した品質を維持することが確認されていなければならない。室温条件を貯法とする製剤では、一定範囲での暴露温度の変動が想定されるため、特に、40℃、50℃、60℃といった高温において、一定期間(例えば、1ヶ月間〜6ヶ月間)保存した、いわゆる熱苛酷保管での品質の安定性が確認されていることが推奨されている。 In the present invention, "storage at room temperature" means that the preparation is stored without using a temperature control facility such as a refrigerator, a freezer, or a heat storage container, for a period from manufacture of the preparation to use. Such pharmaceutical preparations that can be stored at room temperature must be confirmed to maintain stable quality for a predetermined period of time under the storage conditions. For formulations that store at room temperature conditions, fluctuations in the exposure temperature within a certain range are assumed, so especially at high temperatures such as 40 ° C., 50 ° C., 60 ° C., for a fixed period (for example, 1 month to 6 months) It is recommended that the stability of the stored quality in so-called heat and severe storage be confirmed.
本発明において、「製剤が安定」、「品質が安定」または「製剤品質が安定」とは、重要な製剤特性及び/又は製品品質が良好に維持されること、例えば、製剤中に含有される有効成分が化学的に安定であること、及び、凍結乾燥体を注射用水等で再溶解する際の溶解性が良好に維持されることなど、製剤が物理的にも安定であること、を意味する。有効成分が安定であるとは、有効成分を含む凍結乾燥製剤中で、当該有効成分が、含量低下、活性低下、純度低下、分解物の生成(類縁物質の生成)などが少ないことなどを意味する。 In the present invention, "stable formulation", "stable quality" or "stable formulation quality" means that important formulation characteristics and / or product quality are well maintained, for example, contained in the formulation It means that the preparation is physically stable, such as that the active ingredient is chemically stable and that the solubility upon re-dissolving the lyophilizate with water for injection and the like is well maintained. Do. The stability of the active ingredient means that the content of the active ingredient in the freeze-dried preparation containing the active ingredient is reduced in content, activity, purity, generation of decomposition products (formation of related substances), etc. Do.
更に、このような凍結乾燥製剤の化学的安定性や物理的特性・安定性に影響を及ぼす可能性のある特性として、凍結乾燥体の外観(色、形状等)、含有水分量等の物性も挙げることができ、これらの物性も重要な製剤特性とみなすことができる。即ち、凍結乾燥製剤の安定性試験を経てもこのような物理的特性の少なくとも一つ,好ましくは全てが良好に保持されていることが望ましい。例えば、外観形状は、凍結乾燥体の再溶解性に影響する。また、凍結乾燥工程で生じる形状変化は水分除去効率に影響し、変化が生じると水分が適切に除去されず、製造時の水分含量が多くなる可能性が高くなる。また、水分含量が多くなると凍結乾燥体の主基材のガラス転移温度を低下させ、主薬の化学的安定性が低下する可能性、また、製剤保管時の形状変化が生じる可能性が高くなる。このように、凍結乾燥体の外観形状と水分含量は、密接に関連して製剤の重要品質に影響を及ぼす可能性のある製剤特性であり、安定性や溶解性などの重要な製品品質を確保する上で指標となる。 Furthermore, as properties that may affect the chemical stability, physical properties, and stability of such a lyophilized preparation, physical properties such as appearance (color, shape, etc.) of the freeze-dried body, and water content are also included. These physical properties can also be regarded as important formulation properties. That is, it is desirable that at least one, preferably all of such physical properties be well maintained even after stability testing of the lyophilized formulation. For example, the appearance shape affects the resolubility of the lyophilisate. In addition, the shape change caused in the lyophilization process affects the water removal efficiency, and when the change occurs, the water is not appropriately removed, and the possibility of increasing the water content at the time of production is increased. In addition, when the water content increases, the glass transition temperature of the main base material of the lyophilizate decreases, the chemical stability of the main agent may decrease, and the shape change may occur during storage of the preparation. Thus, the appearance shape and the water content of the lyophilizate are the formulation characteristics that may closely relate to the important quality of the formulation, ensuring the important product quality such as stability and solubility. It will be an indicator on
常温(25℃)での保存安定性を確保するためには、製品のガラス転移温度は常温より20℃ほど高い、45℃以上であることが望ましいとされる(F. Franksら「蛋白質・核酸・酵素」p.810-816, 41(6), 1996)。精製白糖のガラス転移温度は、上述の通り、水分0%で70℃前後、保有水分が1%では40〜50℃、2%では30〜40℃と考えられる。そのため、精製白糖を主成分とする凍結乾燥製剤が、室温(25℃)での保存安定性を確保するためには、凍結乾燥体の含水率としては1%以下であることが望ましい。 In order to ensure storage stability at normal temperature (25 ° C.), it is desirable that the glass transition temperature of the product is 45 ° C. or higher, which is about 20 ° C. higher than normal temperature (F. Franks et al. “Protein / Nucleic Acid Enzymes, pp. 810-816, 41 (6), 1996). As described above, the glass transition temperature of purified sucrose is considered to be around 70 ° C. at 0% moisture, 40 to 50 ° C. at 1% retained water, and 30 to 40 ° C. at 2%. Therefore, in order to ensure storage stability at room temperature (25 ° C.), it is preferable that the freeze-dried preparation having purified sucrose as a main component has a water content of 1% or less as the freeze-dried product.
本明細書において、数値の記載に「約」が付加されている場合、明示された数値の上下30%の範囲が許容されることを意味する。ここで、「約」が数値範囲の記載に付加された場合、前記した許容される範囲は、下限の数値の下30%から上限の値の上30%までが許容されることを意味する。許容される範囲は、好ましくは20%、より好ましくは15%、さらに好ましくは10%、さらにより好ましくは5%である。 In the present specification, when “about” is added to the description of numerical values, it means that a range of 30% above and below the explicitly indicated numerical values is permitted. Here, when “about” is added to the description of the numerical range, the above-mentioned acceptable range means that 30% below the lower limit value to 30% above the upper limit value is acceptable. The acceptable range is preferably 20%, more preferably 15%, still more preferably 10%, even more preferably 5%.
次に、本発明の凍結乾燥製剤の各成分について詳細に説明する。 Next, each component of the freeze-dried preparation of the present invention will be described in detail.
本発明の凍結乾燥製剤は、有効成分としては、様々なペプチド性薬物を用いることができるが、好ましくはカルペリチドである。本明細書中において、「カルペリチド」とは、28個のアミノ酸:SLRRSSCFGG RMDRIGAQSG LGCNSFRY(配列番号1)からなるペプチドホルモンであり、α―ヒト型心房性ナトリウム利尿ペプチド(「α―hANP」又は、単に「hANP」とも表記される)とも呼ばれる。カルペリチドは、例えば、生体に由来する組織からの抽出・精製、遺伝子組み換え法等による生物工学的合成、ペプチドの固相合成法のような化学合成等、公知の種々の方法により製造することができる(例えば、再表01/85945号公報等参照)。また、カルペリチドを1バイアル中に1mg含有する、冷暗所保存の凍結乾燥製剤が、「ハンプ注射用1000」として、販売されている。本発明の凍結乾燥製剤においても、生理活性ペプチドとしてカルペリチドを用いる場合、1バイアル当たりの含有量を1mgとするのが好ましい。 The freeze-dried preparation of the present invention can use various peptidic drugs as an active ingredient, but is preferably carperitide. In the present specification, “carperitide” is a peptide hormone consisting of 28 amino acids: SLRRSSCFGG RMDRIGAQSG LGCNSFRY (SEQ ID NO: 1), and α-human atrial natriuretic peptide (“α-hANP” or simply Also referred to as "hANP". Carperitide can be produced by various known methods such as extraction / purification from a tissue derived from a living organism, biotechnological synthesis by genetic recombination, etc., chemical synthesis such as solid phase synthesis of peptide, etc. (For example, the re-listed 01/85945 gazette etc. reference). In addition, a freeze-dried lyophilized preparation containing 1 mg of carperitide in one vial is marketed as "Hump injection 1000". Also in the freeze-dried preparation of the present invention, when using carperitide as a physiologically active peptide, the content per vial is preferably 1 mg.
本発明の凍結乾燥剤には、安定化剤として、所定量の精製白糖を含有する。本発明の精製白糖は、第十六改正日本薬局方に収載されている精製白糖を好適に使用することができる。精製白糖は、本発明の凍結乾燥製剤における有効成分ペプチドに、常温保存時の化学的安定性を与え、かつ、その他の製剤品質や製剤特性に悪影響を及ぼさない外観及び最終水分含有量を達成できる添加量である必要がある。凍結乾燥工程において、溶解液の水分は液面(凍結乾燥体の上部)のみから蒸発するため、水分除去の効率は容器内の固体成分の深さに大きな影響を受ける。容器内の固体成分が浅い場合、水分が効率よく除去され易い。一方で、容器内の固形成分が深い場合水分が除去されにくくなり、最終的な凍結乾燥体の含有水分量が高くなる可能性がある。すなわち、凍結乾燥体の物理的安定性は、凍結乾燥に用いられる容器の胴部の内部断面積に対する精製白糖の含有量に依存する。本発明において、容器の内部断面積に対する精製白糖の含有量は、約0.50〜1.85mg/mm2であり、好ましくは約0.65〜1.60mg/mm2であり、より好ましくは約0.75〜1.35mg/mm2、さらにより好ましくは約1.30mg/mm2である。 The lyophilizer of the present invention contains a predetermined amount of purified sucrose as a stabilizer. As the refined white sugar of the present invention, refined white sugar listed in the 16th revised Japanese Pharmacopoeia can be suitably used. Purified sucrose can provide the active ingredient peptide in the freeze-dried preparation of the present invention with chemical stability during storage at room temperature, and achieve an appearance and final water content that does not adversely affect other preparation quality and properties. It needs to be added. In the lyophilization process, the water content of the solution evaporates only from the liquid surface (upper part of the lyophilizate), so the efficiency of water removal is greatly affected by the depth of the solid component in the container. When the solid component in the container is shallow, water can be efficiently removed. On the other hand, when the solid component in the container is deep, water may be difficult to remove, and the water content of the final freeze-dried product may be high. That is, the physical stability of the lyophilisate depends on the content of refined sucrose with respect to the internal cross-sectional area of the barrel of the container used for lyophilization. In the present invention, the content of refined sucrose with respect to the internal cross-sectional area of the container is about 0.50 to 1.85 mg / mm 2 , preferably about 0.65 to 1.60 mg / mm 2 , more preferably It is about 0.75 to 1.35 mg / mm 2 , even more preferably about 1.30 mg / mm 2 .
精製白糖の、凍結乾燥体当りの含有量は、容器のサイズに応じて適宜選択される。例えば、容器として、内径22.1mmの円筒形バイアルを採用した場合の、凍結乾燥体当りの精製白糖量は、通常約200〜700mgであり、好ましくは約250〜600mgであり、より好ましくは約300〜500mgであり、さらにより好ましくは、約500mgである。 The content of purified white sugar per freeze-dried product is appropriately selected according to the size of the container. For example, when a cylindrical vial with an inner diameter of 22.1 mm is employed as a container, the amount of refined sucrose per lyophilizate is usually about 200 to 700 mg, preferably about 250 to 600 mg, and more preferably about 300. 500 mg, and even more preferably about 500 mg.
本発明の凍結乾燥製剤に用いられる容器は、容器の下方部に胴ストレート部を含むものであり、凍結乾燥操作の温度変化により、変質や変形を生じないものであれば、バイアル、アンプル、注射用シリンジ等、様々なものを使用することができる。胴ストレート部分の断面は様々な形であってよく、例えば、四角形、六角形などの多角形(多角柱バイアル)でもよく、円形(円柱バイアル)であっても良い。容器の大きさとしては、凍結乾燥が可能な大きさであれば特に制限はないが、通常利用される円筒形バイアルの内径は12mm〜50mm程度であり、採用する精製白糖量に応じて適切な内径のバイアルを選択することができる。例えば、精製白糖を300mg用いる場合、内径が約14.6〜29mm(好ましくは、約16〜24mm)の円筒形バイアルが採用される。また、精製白糖として500mgを用いる場合、内径が約19〜34mm(好ましくは、約21〜31.4mm)の円筒形バイアルを用いることができる。 The container used for the freeze-dried preparation of the present invention includes a barrel straight portion in the lower part of the container, and if it does not cause deterioration or deformation due to temperature change of the lyophilization operation, vial, ampoule, injection A variety of syringes and the like can be used. The cross section of the barrel straight portion may have various shapes, for example, may be polygonal (polygonal pillar vial) such as square or hexagonal, or may be circular (cylindrical vial). The size of the container is not particularly limited as long as it is a size that allows lyophilization, but the inner diameter of a generally used cylindrical vial is about 12 mm to 50 mm, and is appropriate depending on the amount of refined sucrose employed. An inner diameter vial can be selected. For example, when 300 mg of purified white sugar is used, a cylindrical vial having an inner diameter of about 14.6 to 29 mm (preferably, about 16 to 24 mm) is employed. Moreover, when using 500 mg as refined sucrose, a cylindrical vial with an inner diameter of about 19 to 34 mm (preferably, about 21 to 31.4 mm) can be used.
<精製白糖以外の添加剤>
本発明の凍結乾燥製剤は、実質的にカルペリチドと精製白糖のみからなる製剤であってもよく、また、必要に応じて、その他の成分(精製白糖以外の安定化剤、緩衝剤、pH調整剤、界面活性剤、溶解補助剤、酸化防止剤、無痛化剤、等張化剤など)をさらに含有しても良い。これら、主薬と精製白糖以外の成分の含有量としては、凍結乾燥体のガラス転移温度に、実質的に影響しない、あるいは、該影響が小さい量、および/もしくは精製白糖による主薬の安定化効果を低下させない量である必要があり、、当該成分を用いる場合の含有量は、その総量として、好ましくは、精製白糖の20重量%以下であり、より好ましくは10重量%以下であり、さらに好ましくは5重量%以下であり、さらにより好ましくは、1重量%以下である。
<Additives other than refined white sugar>
The freeze-dried preparation of the present invention may be a preparation consisting essentially of carperitide and purified white sugar, and if necessary, other components (a stabilizer other than purified white sugar, a buffer, a pH adjuster, etc. The composition may further contain a surfactant, a solubilizing agent, an antioxidant, a soothing agent, a tonicity agent, and the like. The content of components other than the main drug and purified white sugar does not substantially affect the glass transition temperature of the freeze-dried product, or an amount having a small influence on the glass transition temperature, and / or the stabilizing effect of the main drug by the purified white sugar The total amount of the content when using the component is preferably 20% by weight or less, more preferably 10% by weight or less, and further preferably, the total amount thereof is not reduced. It is at most 5 wt%, even more preferably at most 1 wt%.
精製白糖以外の安定化剤としては、トレハロース、ラクトース、マルトースなどの精製白糖と同じく二糖類に属する糖、従来安定化剤として用いられていたグリシン、アラニン、アルギニン、リジン、ヒスチジン、メチオニンなどのアミノ酸、ヘパリン、デキストラン硫酸などの多糖類、ソルビトール、マンニトールなどの糖アルコール、卵アルブミン、血清アルブミンなどの蛋白質などを好適に使用できる。これらのうち、二糖類が好ましく、とりわけトレハロースが好ましい。これらの精製白糖以外の安定化剤の添加量は特に制限されないが、精製白糖の20重量%以下が好ましく、10重量%以下がより好ましい。 As a stabilizer other than purified white sugar, a sugar belonging to a disaccharide as well as purified white sugar such as trehalose, lactose and maltose, amino acids such as glycine, alanine, arginine, lysine, histidine and methionine which have been conventionally used as a stabilizer Preferably, polysaccharides such as heparin and dextran sulfate, sugar alcohols such as sorbitol and mannitol, proteins such as egg albumin and serum albumin can be suitably used. Among these, disaccharides are preferred, and trehalose is particularly preferred. Although the addition amount of stabilizers other than these refined sucrose is not restrict | limited in particular, 20 weight% or less of refined sucrose is preferable, and 10 weight% or less is more preferable.
本発明で用いられる緩衝剤としては、例えばリン酸緩衝液、クエン酸緩衝液、酢酸緩衝液、グリシン・塩酸緩衝液などが挙げられる。緩衝剤は、必要に応じ、再溶解後の水溶液のpHを調整し、カルペリチドの溶解性や安定性を保つために使用することができる。緩衝剤としては、再溶解後の水溶液のpHが4.0〜6.5となるものが好ましく、また、カルペリチドの塩析を防止するため、ナトリウム塩やカリウム塩などの電解質を含有しないものが好ましく、特に好ましい緩衝液として、例えば、グリシン・塩酸緩衝液が挙げられる。緩衝剤の添加量は、凍結乾燥製剤を製造する際の凍結乾燥直前の溶解液中の濃度が、1〜100mMの範囲となるようにするのが好ましい。 As a buffer used by this invention, a phosphate buffer, a citrate buffer, an acetate buffer, a glycine * hydrochloric acid buffer etc. are mentioned, for example. The buffer can be used to adjust the pH of the re-dissolved aqueous solution, as needed, to maintain the solubility and stability of carperitide. As the buffer, one having a pH of 4.0 to 6.5 after re-dissolution is preferable, and one that does not contain an electrolyte such as sodium salt or potassium salt to prevent salting out of carperitide Preferred and particularly preferred buffers include, for example, glycine / hydrochloric acid buffer. The amount of buffer added is preferably such that the concentration in the solution immediately before lyophilization in the preparation of the lyophilised formulation is in the range of 1 to 100 mM.
本発明で用いられる界面活性剤としては、例えばポリソルベート20、ポリソルベート80、プルロニックF−68、ポリエチレングリコールなどが挙げられ、二種以上を併用してもよい。界面活性剤として、ポリソルベート系界面活性剤が好ましく、とりわけポリソルベート80が好ましい。界面活性剤は、例えば、水溶液中でのカルペリチドの、容器への吸着を防止するため、必要に応じて添加することができる。界面活性剤の添加量は、凍結乾燥製剤を製造する際の凍結乾燥直前の溶解液中の濃度が、0.001〜2.0重量%の範囲であるのが好ましい。 As surfactant used by this invention, polysorbate 20, polysorbate 80, Pluronic F-68, polyethyleneglycol etc. are mentioned, for example, You may use 2 or more types together. As the surfactant, polysorbate surfactants are preferred, and polysorbate 80 is particularly preferred. Surfactants can be added as needed, for example, to prevent adsorption of carperitide in an aqueous solution to the container. The amount of surfactant added is preferably in the range of 0.001 to 2.0% by weight in the solution immediately before lyophilization when producing the lyophilized formulation.
本発明の凍結乾燥用組成物には、その再溶解液のpHを調整するため、さらに酸、又は、塩基を、pH調整剤として含んでもよい。本発明の凍結乾燥製剤にさらに添加してもよい酸としては、例えば、無機酸(例えば、塩酸、リン酸、臭化水素酸、硫酸)、有機酸(例えば、ギ酸、酢酸、プロピオン酸、フマル酸、マレイン酸、コハク酸、酒石酸、クエン酸、リンゴ酸、蓚酸、安息香酸、メタンスルホン酸、ベンゼンスルホン酸)等から選択される1種又は複数種の酸が挙げられる。 The lyophilization composition of the present invention may further contain an acid or a base as a pH adjuster in order to adjust the pH of the redissolved solution. Examples of the acid that may be further added to the freeze-dried preparation of the present invention include, for example, inorganic acids (eg, hydrochloric acid, phosphoric acid, hydrobromic acid, sulfuric acid), organic acids (eg, formic acid, acetic acid, propionic acid, fumaric acid) Examples include one or more acids selected from acids, maleic acid, succinic acid, tartaric acid, citric acid, malic acid, oxalic acid, benzoic acid, methanesulfonic acid, benzenesulfonic acid) and the like.
なかでも塩酸、酢酸が好ましい。これらの酸の量は特に限定されず、凍結乾燥用組成物の再溶解液のpHを所定範囲に調整し得る量で当該凍結乾燥用組成物に添加すればよい。
本発明で用いられる酸化防止剤としては、亜硫酸ナトリウム、亜硫酸水素ナトリウム、ピロ亜硫酸ナトリウム、L-システイン塩酸塩、チオグリコール酸などの自己酸化性(還元性)を有する物質、メチオニンなどのアミノ酸類が挙げられる。但し、カルペリチドと還元性物質が共存する場合、ペプチドがジスルフィド結合の還元開裂により分解する可能性がある。そのため、ペプチドの酸化を防止する物質として、好ましくはメチオニンなどのアミノ酸類が挙げられ、精製白糖1重量部に対し、0.001〜0.1重量部の範囲で用いることが好ましい。
Among them, hydrochloric acid and acetic acid are preferable. The amount of these acids is not particularly limited, and may be added to the lyophilization composition in such an amount that the pH of the re-dissolution solution of the lyophilization composition can be adjusted within a predetermined range.
As the antioxidant used in the present invention, substances having self-oxidation (reducibility) such as sodium sulfite, sodium bisulfite, sodium pyrosulfite, L-cysteine hydrochloride, thioglycolic acid and the like, amino acids such as methionine, etc. It can be mentioned. However, when carperitide and a reducing substance coexist, the peptide may be degraded by reductive cleavage of a disulfide bond. Therefore, as a substance which prevents oxidation of a peptide, Preferably amino acids, such as a methionine, are mentioned, It is preferable to use in 0.001-0.1 weight part with respect to 1 weight part of refinement | purification sucroses.
本発明で用いられる等張化剤としては、例えば、ブドウ糖などの単糖類、マンニトールなどの糖アルコール類、塩化ナトリウムなどの無機塩類が挙げられ、好ましくはブドウ糖などの単糖類もしくはマンニトールなどの糖アルコール類が挙げられ、精製白糖1重量部に対し、0.001〜0.2重量部の範囲で用いることが好ましい。
本発明で用いられる無痛化剤としては、例えばベンジルアルコール、クロロブタノールなどのアルコール類や、塩酸リドカインなどが挙げられ、凍結乾燥製剤を製造する際の溶解液中の濃度が、0.001〜2.0重量%の範囲で用いることが好ましい。
Examples of the tonicity agent used in the present invention include monosaccharides such as glucose, sugar alcohols such as mannitol, and inorganic salts such as sodium chloride, preferably monosaccharides such as glucose or sugar alcohols such as mannitol. It is preferable to use it in the range of 0.001 to 0.2 parts by weight with respect to 1 part by weight of purified sucrose.
The soothing agent used in the present invention includes, for example, alcohols such as benzyl alcohol and chlorobutanol, lidocaine hydrochloride and the like, and the concentration in the solution at the time of producing the freeze-dried preparation is 0.001 to 2 It is preferable to use in the range of 0.1% by weight.
<凍結乾燥製剤>
本発明の凍結乾燥製剤は、公知の方法で製造することができる。
例えば所定量のカルペリチド又はその塩、と、所定量の精製白糖を、所定量の水又は適当な水性溶媒(例えば、水とアルコールの混合物)に溶解して溶解液を調製し、所望により酸を添加して水性液のpHを調整し、さらに、フィルター(例えば、孔径0.22μmの除菌フィルター)等を用いて除菌濾過することにより得られる、無菌の溶解液をバイアル又はアンプルに注入し、この容器を凍結乾燥して固体状とすることにより、凍結乾燥剤を得ることができる。
<Lyophilized formulation>
The lyophilized preparation of the present invention can be produced by known methods.
For example, a solution is prepared by dissolving a predetermined amount of carperitide or a salt thereof and a predetermined amount of purified sucrose in a predetermined amount of water or a suitable aqueous solvent (eg, a mixture of water and alcohol), and optionally an acid Add the solution to adjust the pH of the aqueous solution, and inject a sterile solution obtained by filtration and sterilization filtration using a filter (for example, a 0.22 μm pore diameter sterilization filter) into a vial or ampoule. The lyophilizing agent can be obtained by lyophilizing this container to make it solid.
上記凍結乾燥剤の調製における溶解液の調製は、公知の方法に従って、有効成分ペプチドおよび精製白糖を水又は水性溶媒(たとえば、水とアルコールの混合物)に溶解し、必要に応じて酸を添加してpHを調整すればよい。また、有効成分ペプチドおよび精製白糖を溶解させる順序は特に限定されない。 In preparation of the above-mentioned lyophilizer, the solution is prepared by dissolving the active ingredient peptide and purified sucrose in water or an aqueous solvent (for example, a mixture of water and alcohol) and adding an acid as necessary according to a known method. PH should be adjusted. In addition, the order of dissolving the active ingredient peptide and purified sucrose is not particularly limited.
上記凍結乾燥剤の調製において、水性液中における有効成分ペプチドの濃度は、最終製品において医薬品として承認された用量となるように適宜設定されるが、通常0.01mg/mL〜5mg/mLである。カルペリチドを1mg含む凍結乾燥製剤において、バイアル当たりの溶解液の充填量が5mLの場合、溶解液のカルペリチド濃度は0.2mg/mLに調整される。 In the preparation of the above-mentioned lyophilizer, the concentration of the active ingredient peptide in the aqueous liquid is appropriately set to a pharmaceutically acceptable dose in the final product, but is usually 0.01 mg / mL to 5 mg / mL. . In a lyophilised formulation containing 1 mg of carperitide, the carperitide concentration of the lysate is adjusted to 0.2 mg / mL if the loading of lysate per vial is 5 mL.
上記の凍結乾燥に供される水性溶液中の精製白糖の濃度は、他の添加物の組成にもよるが、下限は通常約10mg/mL以上である。凍結乾燥に供される溶液に含まれる固形成分の濃度は、凍結乾燥工程の水分除去効率に影響を与えるため、凍結乾燥終了時に低い水分含量を達成するためには、精製白糖濃度は低いことが望ましい。溶解液中の精製白糖濃度の上限としては通常140mg/mL以下であり、好ましくは125mg/mL以下である。 The lower limit of the concentration of purified sucrose in the aqueous solution to be subjected to the above-mentioned lyophilization depends on the composition of the other additives, but is usually about 10 mg / mL or more. The concentration of solid components contained in the solution to be subjected to lyophilization affects the water removal efficiency of the lyophilization process. Therefore, in order to achieve a low water content at the end of lyophilization, the purified sucrose concentration should be low. desirable. The upper limit of the concentration of purified sucrose in the solution is usually 140 mg / mL or less, preferably 125 mg / mL or less.
滅菌に用いるフィルターは、ポアサイズ0.22μm以下の滅菌用フィルターを使用するのが好ましい。滅菌用フィルターとしては、例えば、デュラポア(登録商標、日本ミリポア株式会社製)またはザルトポア2(登録商標、ザルトリウス株式会社製)などが挙げられる。 The filter used for sterilization is preferably a sterilizing filter with a pore size of 0.22 μm or less. Examples of the sterilization filter include Durapore (registered trademark, manufactured by Nippon Millipore Co., Ltd.) or Zaltopore 2 (registered trademark, manufactured by Sartorius, Inc.).
上記の工程により調整された溶解液は、容器に一定量充填され、当該充填された容器が凍結乾燥に供される。この際の容器当たりの溶解液の充填量は、容器のサイズに依存して変動するが、通常充填液の深さ(液深)が、3mm〜20mm程度(好ましくは5mm〜17mm程度)である。液深が小さすぎると凍結乾燥体が形成されず、逆に大きすぎる場合には、容器下部における水分除去が効率的に進行しない可能性がある。 The solution prepared by the above steps is filled in a fixed amount in a container, and the filled container is subjected to lyophilization. The filling amount of the solution per container at this time varies depending on the size of the container, but the depth (liquid depth) of the filling solution is usually about 3 mm to 20 mm (preferably about 5 mm to 17 mm) . If the liquid depth is too small, a lyophilizate is not formed, and if it is too large, water removal at the lower part of the container may not proceed efficiently.
凍結乾燥方法としては、例えば、常圧下で冷却凍結する凍結過程、溶質に拘束されない自由水を減圧下で昇華乾燥する一次乾燥過程、溶質固有の吸着水や結晶水を除去する二次乾燥過程の3つの単位操作による方法が挙げられる。凍結過程の冷却温度は−60℃〜−40℃が好ましく、一次乾燥過程の温度は−50℃〜0℃が好ましく、さらに二次乾燥過程の温度は4℃〜40℃が好ましい。一次乾燥過程の真空圧力は0.1〜50Paにコントロールされることが好ましく、特に0.5〜30Paにコントロールされることが好ましい。凍結乾燥後の乾燥庫内は復圧させる。復圧の方法としては、無菌の空気または不活性ガス(例えば、無菌窒素ガス、無菌ヘリウムガスなど)を庫内に送入して約60〜90kPaまで一次復圧し、次いで必要に応じて、更に復圧(二次復圧)する方法が好ましい。バイアルの打栓は、一次復圧後に行うのが好ましい。 As a lyophilization method, for example, a freezing process of freezing and freezing under normal pressure, a primary drying process of sublimating and drying free water not restricted by a solute under a reduced pressure, and a secondary drying process of removing adsorbed water and water of crystallization inherent to a solute There are three unit operation methods. The cooling temperature in the freezing process is preferably -60C to -40C, the temperature in the primary drying process is preferably -50C to 0C, and the temperature in the secondary drying process is preferably 4C to 40C. The vacuum pressure in the primary drying process is preferably controlled to 0.1 to 50 Pa, particularly preferably 0.5 to 30 Pa. The pressure in the drying cabinet after lyophilization is reduced. As a method of repressurization, aseptic air or inert gas (for example, sterile nitrogen gas, sterile helium gas, etc.) is sent into the chamber to temporarily repressurize to about 60 to 90 kPa, and then, if necessary, further The method of repressurization (secondary repressurization) is preferred. It is preferable to stop the vial after primary pressure reduction.
<製剤の使用>
本発明の凍結乾燥製剤は、使用前に用時注射用水あるいは輸液(例えば、生理食塩液、ブドウ糖液等)に再溶解して、注射、点滴等に用いることができる。但し、カルペリチドは生理食塩水で溶解する場合、溶解条件が適切でないとゲル化する恐れがあるため、再溶解後の薬物濃度の調整や使用時の状態への留意を要する。また、ブドウ糖液は、患者が糖尿病又はそのリスクを有する場合に、使用が制限される可能性がある。そのため、本発明の凍結乾燥製剤の再溶解には注射用水を用いることが望ましい。
<Use of preparation>
The freeze-dried preparation of the present invention can be redissolved in water for injection or infusion (eg, physiological saline, glucose solution etc.) before use and used for injection, infusion and the like. However, when dissolved in physiological saline, carperitide may be gelled if the dissolution conditions are not appropriate, so it is necessary to adjust the drug concentration after reconstitution and to pay attention to the state at the time of use. In addition, glucose solution may be limited in use if the patient has diabetes or its risk. Therefore, it is desirable to use water for injection to redissolve the lyophilized preparation of the present invention.
本発明の凍結乾燥剤は、例えば、皮下注射用組成物をはじめとして、静脈注射用組成物、筋肉注射用組成物、点滴注射用組成物、無針注射用組成物等の種々の注射用組成物として用いることができる。この場合、注射時の有効成分ペプチドの注射用組成物中の濃度(凍結乾燥剤の場合は、再溶解濃度)は、通常約0.01mg/mL〜60mg/mL、好ましくは約0.05mg/mL〜20mg/mLである。 The lyophilizing agent of the present invention is, for example, various compositions for injection such as composition for subcutaneous injection, composition for intravenous injection, composition for intramuscular injection, composition for drip injection, composition for needle-free injection It can be used as a thing. In this case, the concentration of the active ingredient peptide in the composition for injection at the time of injection (in the case of a lyophilizing agent, the resolubilizing concentration) is usually about 0.01 mg / mL to 60 mg / mL, preferably about 0.05 mg / mL. mL-20 mg / mL.
本発明の凍結乾燥剤を用時に再溶解して注射に用いる場合、公知の、例えば濾過滅菌等の無菌調製法により上記水性液を調製するのが好ましい。また本発明の凍結乾燥剤を調製する前に、糖類および界面活性剤、又は糖類、界面活性剤および必要に応じてその他の添加物との混合物を、予め脱パイロジェン処理等の除菌処理を施してから用いることもできる。 When the lyophilizer of the present invention is redissolved at the time of use and used for injection, it is preferable to prepare the above-mentioned aqueous liquid by a known aseptic preparation method such as filter sterilization. In addition, before preparing the lyophilizer of the present invention, saccharides and surfactants, or a mixture of saccharides, surfactants, and other additives if necessary, are subjected to sterilization treatment such as depyrogenation in advance. Can also be used.
さらに、本発明の凍結乾燥製剤は、急性心不全の予防剤又は治療剤のみならず、血圧の上昇や心臓への負荷が関係する疾患の予防剤又は治療剤としても有利に使用できる。
本発明の凍結乾燥製剤は、単剤として優れた血圧降下作用、心臓保護作用を有し、心疾患の予防剤又は治療剤として有効な作用を示すが、さらに他の医薬成分と併用(多剤併用)することもできる。
Furthermore, the freeze-dried preparation of the present invention can be advantageously used not only as a preventive or therapeutic agent for acute heart failure, but also as a prophylactic or therapeutic agent for diseases associated with elevation of blood pressure and load on the heart.
The freeze-dried preparation of the present invention has an excellent blood pressure lowering action and a cardioprotective action as a single agent, and exhibits an action effective as a preventive or therapeutic agent for heart disease, but it is used in combination with other pharmaceutical ingredients (multidrug It can also be used in combination.
以下、実施例を用いて、本発明を具体的に説明する。実施例に示されたものは、本発明の実施形態の一例であり、本発明はこれに限定されるものではない。 本実施例においては、凍結乾燥製剤の容器として、「ハンプ注射用1000」用円筒形ガラスバイアル(胴外径24.5 mm、内径22.1mm)を採用した。 Hereinafter, the present invention will be specifically described using examples. What is shown in the examples is one example of the embodiment of the present invention, and the present invention is not limited thereto. In this example, a cylindrical glass vial (body outer diameter: 24.5 mm, inner diameter: 22.1 mm) for "Hump injection 1000" was adopted as a container for the freeze-dried preparation.
<実施例1:精製白糖の配合条件の検討(白糖プラセボ製剤)>
主な製剤成分として精製白糖が配合され、良好な製品特性を有する凍結乾燥製剤の製剤設計を見出すため、製剤処方及び製造工程(凍結乾燥用液)における精製白糖の配合条件(以下、「白糖配合条件」)を検討した。
本試験における精製白糖量の検討範囲は以下の理由により定めた。カルペリチド現行製品(製品名:「ハンプ注射用1000」)の用法用量においては、製剤1本(バイアル1本)を注射用水10 mLで再溶解することから、本検討においては、医療現場での投薬準備の効率性を維持もしくは向上する観点から、再溶解液の種類は変更せず、量は現行製品以下(10 mL以下)であることが望ましい。一方、医療現場における調剤において、再溶解後の溶液をシリンジ等で抜き取った後の、製剤容器への付着などによる溶液の残存率(残液率)は、溶液量が小さいほど大きくなるため、製品設計においては、この残液率ができるだけ小さくなるように再溶解液量を設定する必要がある。したがって、今回の製品設計においては、再溶解液量を1〜10 mLの範囲に設定した。
また、カルペルチド製剤は、医療現場において注射用水による再溶解後、輸液による希釈なしで直接投与される場合があるため、溶解後は等張である必要がある。精製白糖を主成分とする製剤の場合、等張確保に要する溶解液量は、精製白糖量の約10倍(精製白糖100 mgに対して注射用水約1 mL)である。今回の製品設計において、注射用水量を1〜10 mLとしたことから、精製白糖量の検討範囲は100〜1000 mgとした。
本検討においては、製剤1本(バイアル1本)あたりの精製白糖量(以下、「白糖量」)、凍結乾燥用の溶液における精製白糖の濃度(以下、「白糖濃度」)を変動要因として、また、凍結乾燥体の外観形状及び水分を製剤品質特性として評価を行った。
なお、本試験は、凍結乾燥体の外観、水分などの物理的特性に主眼を置くため、検討対象とするカルペリチド含有量と精製白糖量の比率から、カルペリチドによるこれら物理的特性への影響はほとんど無視できると判断し、本試験は、カルペリチドを含有しない製剤(白糖プラセボ製剤)を用いて実施した。
<Example 1: Examination of compounding conditions of purified sucrose (sucrose placebo preparation)>
In order to find a formulation design of a freeze-dried formulation having refined sucrose incorporated as the main formulation component and having good product characteristics, the formulation conditions of refined sucrose in formulation formulation and manufacturing process (liquid for lyophilization) (hereinafter referred to as “blending sucrose” I examined the condition ").
The examination range of the amount of refined white sugar in this test was determined for the following reasons. In the case of the dosage regimen of Carperitide current product (product name: "Hump 1000 for injection"), one preparation (one vial) is redissolved with 10 mL of water for injection. From the viewpoint of maintaining or improving the efficiency of preparation, it is desirable that the type of re-dissolution be unchanged and that the amount be less than or equal to the current product (10 mL or less). On the other hand, in the preparation at a medical site, the remaining rate (residual solution rate) of the solution due to adhesion to the preparation container after withdrawal of the solution after re-dissolution with a syringe etc. increases as the solution amount decreases. In design, it is necessary to set the amount of re-dissolution so that this residual liquid rate becomes as small as possible. Therefore, in this product design, the amount of re-dissolution was set in the range of 1 to 10 mL.
In addition, carpertide preparations need to be isotonic after dissolution, as they may be directly administered without dilution by infusion after being redissolved in water for injection in a medical setting. In the case of a preparation containing purified white sugar as the main component, the amount of solution required to ensure isotonicity is about 10 times the amount of purified white sugar (about 1 mL of water for injection relative to 100 mg of purified white sugar). In this product design, the amount of water for injection was set to 1 to 10 mL, so the examination range of the amount of purified white sugar was set to 100 to 1000 mg.
In the present study, the amount of purified sucrose (hereinafter, “the amount of sucrose”) per preparation (one vial) and the concentration of the purified sucrose in the solution for lyophilization (hereinafter, “concentration of sucrose”) are variable factors. In addition, the appearance shape and the water content of the freeze-dried product were evaluated as formulation quality characteristics.
In addition, since this test focuses on the physical properties such as the appearance and moisture of the lyophilizate, the ratio of the content of carperitide to the study and the amount of refined sucrose to be studied makes the influence of carperitide on these physical properties almost negligible. Judging that this was negligible, this test was conducted using a preparation containing no carperitide (sucrose placebo preparation).
(1)白糖プラセボ製剤の調製(配合例1〜17)
精製白糖(日本薬局方、塩水港精糖株式会社)を、表1の各配合例における所定の白糖濃度となるように精製水に溶解した。白糖溶液をフィルター(Stericup-GV 0.22μm、PVDF、Millipore Corporation)にて濾過した後、テーハー分注機(FH-10s、株式会社ヒラサワ)またはマイクロスケールピペット(PIPETMAN、GILSON, Inc.など)を用い、同様に所定の充填量となるようにガラスバイアル(胴外径24.5 mm)、大和特殊硝子株式会社)に充填した。充填済バイアルに、ゴム栓(V10-F8 D713 RB2-40、株式会社大協精工)を半打栓した後、凍結乾燥機(RL-30KPs、共和真空株式会社)に搬入し、予備凍結(−50℃設定)、引き続いて真空条件下(20 Pa設定)で凍結乾燥(一次乾燥:−20〜−5℃設定、二次乾燥:40℃設定)を行い、乾燥終了後にバイアル内を、窒素導入により復圧した。バイアルにゴム栓を全打栓した後、巻締機(GAC-01、株式会社稲葉機械製作所)を用いてフリップオフキャップ(APキャップ、20AP7.0H、石田プレス工業株式会社)でバイアルを巻き締めし、配合例1〜17の白糖プラセボ製剤を得た。
(1) Preparation of Sucrose Placebo Preparation (Formulation Examples 1 to 17)
Purified white sugar (Japanese Pharmacopoeia, Saline Port Segarase Co., Ltd.) was dissolved in purified water so as to have a predetermined white sugar concentration in each formulation example of Table 1. After filtering the white sugar solution through a filter (Stericup-GV 0.22 μm, PVDF, Millipore Corporation), use a Teha dispenser (FH-10s, Hirasawa Co., Ltd.) or a microscale pipette (PIPETMAN, GILSON, Inc., etc.) In the same manner, glass vials (body outer diameter: 24.5 mm, Yamato Special Glass Co., Ltd.) were filled in such a manner as to obtain a predetermined filling amount. After half-stopping a rubber stopper (V10-F8 D713 RB2-40, Daikyo Seiko Co., Ltd.) into the filled vial, it is carried into a lyophilizer (RL-30 KPs, Kyowa Vacuum Co., Ltd.) and pre-frozen (- Next, freeze drying (primary drying: -20 to -5 ° C setting, secondary drying: 40 ° C setting) is performed under vacuum conditions (20 Pa setting), and after the drying is completed, the vial is introduced with nitrogen Pressure was released. After all the rubber stoppers have been plugged into the vial, use a clamping machine (GAC-01, Inaba Machine Mfg. Co., Ltd.) to clamp the vial with a flip-off cap (AP cap, 20AP7.0H, Ishida Press Co., Ltd.) The white sugar placebo formulations of Formulation Examples 1 to 17 were obtained.
(2)凍結乾燥製剤の熱苛酷保管後の製剤品質特性の分析
上記(1)で作製した凍結乾燥製剤を40℃75%RHに設定した恒温恒湿槽(LH31-15M型、株式会社ナガノ科学機械製作所)、または、50℃に設定した恒温槽(LH20-01型、株式会社ナガノ科学機械製作所)で1ヶ月間保管した。製剤の製造時、及び、各条件での保管前後に、凍結乾燥体の外観形状及び水分含量を、以下の方法で評価した。
(2) Analysis of preparation quality characteristics of freeze-dried preparation after storage under heat and stress A thermostatic chamber in which the freeze-dried preparation prepared in (1) above is set at 40 ° C. 75% RH (LH 31-15M type, NAGANO SCIENCE CO., LTD. It stored for 1 month in a thermostat (LH20-01 type | mold, Nagano Scientific Machinery Mfg. Co., Ltd.) set to 50 degreeC. At the time of manufacture of the preparation and before and after storage under each condition, the appearance shape and the water content of the lyophilizate were evaluated by the following method.
[方法:凍結乾燥体の外観評価]
凍結乾燥製剤の外観形状を目視観察し、以下の通り3段階で符号判定した。製造時には、無作為に選択した23〜25本を観察した。熱苛酷保管では、各温度での保管前に外観形状が良好なものの中から3本を無作為に選択し、保管前後に同一の製剤を観察した。これらの結果を表2及び表3に示した。
○:良好な形状(正常形状)
△:おおむね良好な形状(正常形状と比較し、軽微な変化のみ認められる)
×:不良な形状(形状不良:正常形状と比較し、著しいシュリンクなどの大きな変化が認められる)。
[Method: Evaluation of appearance of freeze-dried product]
The appearance shape of the freeze-dried preparation was visually observed, and the code was judged in three steps as follows. At the time of manufacture, 23 to 25 randomly selected were observed. In heat and severe storage, before storage at each temperature, three were randomly selected from those with a good appearance shape, and the same formulation was observed before and after storage. The results are shown in Tables 2 and 3.
○: good shape (normal shape)
:: Almost good shape (only slight change is observed compared to the normal shape)
X: Defective shape (defective shape: significant changes such as significant shrinkage are observed as compared to a normal shape).
[方法:凍結乾燥体の水分測定]
凍結乾燥体の10 mg以上を、吸湿低減のための湿度環境下、ガラス製密栓付採取管に秤量し、電量滴定式微量水分測定装置(CA-100型、三菱化学株式会社)により水分量(凍結乾燥体重量の含水率、%)を測定した。各測定時に無作為に選抜した2または3本について測定し、含水率の平均値を表2及び表3に示した。
[Method: moisture measurement of freeze-dried product]
Measure 10 mg or more of the freeze-dried product in a glass stoppered collection tube under a humidity environment to reduce moisture absorption, and use a coulometric titration type trace water content measuring device (CA-100 type, Mitsubishi Chemical Corporation) to measure the water content ( The moisture content (%) of the freeze-dried body weight was measured. It measured about 2 or 3 randomly selected at each measurement, and the average value of the moisture content was shown in Table 2 and Table 3.
[結果] 配合例1〜7の製剤(白糖量1000 mgまたは500mg/バイアル)の製造時、40℃75%RH1ヶ月保管後、50℃1ヶ月保管後の外観形状、含水率を表2に示した。同様に、配合例8〜17(白糖量300 mgまたは100 mg/バイアル)の製剤の外観形状、含水率を表3に示した。各配合例について、良好な製剤品質と判定するに当たり、製造時及び熱苛酷保管の全ての時点において、外観形状が○又は△の評価であり、且つ、含水率が1%以下、であることを判定基準とした。
配合例5〜12の製剤(白糖量500 mg/バイアル(白糖濃度125 mg/mL以下)または300 mg/バイアル)は、製造時、熱苛酷保管後ともに外観、水分の判定基準に適合しており、これらの条件でカルペリチド製剤を製造したとき、熱安定性など、良好な製品特性が確保できることを示す。
一方、配合例1〜4の製剤(白糖量1000 mg/バイアルまたは500 mg/バイアル(白糖濃度160 mg/mL以上)は、いずれも製造時に明らかな外観不良(1割以上の×判定)を生じ、また、製造時の水分は1%以上であり、外観、水分共に判定基準に不適合であった。配合例1及び配合例4の製剤のうち、製造時の外観が良好であった製剤について、熱苛酷保管後の評価を実施したところ、50℃保管で外観不良(判定基準へ不適合)となる検体を認めた。これは、水分が判定基準を満足しない製剤には、その熱安定性に不安があることを示している。
配合例13〜17の製剤(白糖量100 mg/バイアル)は、製造時は外観、水分共に判定基準を満足するが、熱苛酷1ヶ月保存後に水分が1%以上への増加(判定基準への不適合)を認めた。白糖量が少ない製剤では、製剤容器の密栓に使用するゴム栓の保有水分の影響を受け、保管中に水分含量が上昇し、製品特性が変化する可能性が示唆された。
[Results] Table 2 shows the appearance shape and moisture content after storage for one month at 40 ° C. and 75% RH after storage for one month at 40 ° C. and 75% RH at the time of manufacturing the formulations of Formulation Examples 1 to 7 (sucrose amount 1000 mg or 500 mg / vial). The Similarly, the appearance shape and moisture content of the preparations of Formulation Examples 8 to 17 (the amount of sucrose 300 mg or 100 mg / vial) are shown in Table 3. For each formulation example, it is evaluated that the appearance shape is evaluated as ○ or 、 and the moisture content is 1% or less at the time of manufacturing and all heat storage conditions in order to determine that the formulation quality is good. It was taken as the judgment standard.
Formulations of Formulation Examples 5 to 12 (white sugar amount 500 mg / vial (sucrose concentration 125 mg / mL or less) or 300 mg / vial) conform to the appearance and moisture judgment criteria both during heat stress storage at the time of production. When carperitide formulations are produced under these conditions, it is shown that good product properties such as thermal stability can be ensured.
On the other hand, each of the preparations of Formulation Examples 1 to 4 (sucrose amount 1000 mg / vial or 500 mg / vial (sucrose concentration 160 mg / mL or more) causes obvious appearance defects (10% or more x judgment) at the time of production. Also, the moisture at the time of production was 1% or more, and both the appearance and the moisture were not suitable for the judgment criteria. When evaluation after heat and severe storage was carried out, a sample with appearance defect (inappropriate to the judgment standard) was recognized by storage at 50 ° C. This is anxious about the heat stability of the formulation whose water does not satisfy the judgment standard. It shows that there is.
Formulations of Formulation Examples 13 to 17 (Sucrose content 100 mg / vial) satisfy the judgment criteria for both appearance and moisture at the time of manufacture, but increase in moisture to 1% or more after storage for 1 month of heat stress Nonconformity). It was suggested that the preparation with a small amount of white sugar may be affected by the water content of the rubber stopper used for closing the preparation container, the water content may increase during storage, and the product characteristics may change.
※:製造時の外観評価が○判定(外観変化がなし)の製剤を無作為に選抜して各温度下で保管。外観は実測値(製剤3本の判定符号)を記載.−:測定せず.
※: The appearance evaluation at the time of manufacture evaluated the preparation of O judgment (there is no change in appearance) at random, and store it under each temperature. Appearance shows actual measurement value (determination code of 3 preparations). −: Not measured
※:外観評価が○又は△判定(外観変化がなし又は軽微)の製剤を無作為に選抜して各温度下で保管。外観は実測値(製剤3本の判定符号)を記載.−:測定せず. ※: Formulations with appearance evaluation ○ or 判定 (no appearance change or slight) are randomly selected and stored under each temperature. Appearance shows actual measurement value (determination code of 3 preparations). −: Not measured
これらの結果から、凍結乾燥のための容器として胴外径24.5 mm(内径22.1mm)のガラスバイアルを用い、精製白糖を主な固形成分とする凍結乾燥製剤の製造において、外観形状、水分の判定基準を満足する白糖配合条件は、白糖量については300 mg(容器内部断面積当り0.78 mg/mm2)〜500 mg/バイアル(容器内部断面積当り1.30mg/mm2)、白糖濃度については48〜125 mg/mL(充填量は2.5 〜6.25 mL/バイアル)であることが示された。 From these results, using a glass vial with an outer diameter of 24.5 mm (inner diameter: 22.1 mm) as a container for lyophilization, in the manufacture of a lyophilization formulation having purified sucrose as the main solid component, an appearance shape, Sucrose mixing conditions that satisfy the criteria for water content are: 300 mg (0.78 mg / mm 2 per container cross sectional area) to 500 mg / vial (1.30 mg / mm 2 per container internal cross sectional area) for sucrose content The sucrose concentration was shown to be 48-125 mg / mL (filling volume 2.5-6.25 mL / vial).
当該条件において、製造時の品質特性に着目してみると、バイアル当りの精製白糖量が多い、又は、充填液の白糖濃度が高い場合には、製造時の外観不良の割合が高く、含有水分も高い傾向があった。これらの凍結乾燥体では凍結乾燥工程における水分除去が正常に進行しなかったものと考えられる。凍結乾燥工程の水分除去は、凍結した水分が昇華し、凍結乾燥体の上面から放出されることで進行するため、凍結乾燥体上面の面積(容器の内部断面積)当たりの白糖量が少ないほど、水分の除去効率は高くなると考えられる。本検討においても、同一サイズのバイアルにおいて、白糖量が少ないほど、及び、白糖濃度が低いほど、製造時の含水率が低い傾向があった。従って、製造時に良好な製剤品質特性を確保するためには、容器内部断面積当たりの精製白糖量を少なくする(通常約1.85mg/mm2以下)する必要がある。また、同様の目的で、凍結乾燥に用いる充填液の濃度は、配合例4(160mg/mL)の場合の品質特性が、基準にわずかに届かなかったことを考慮すると、140mg/mL以下程度であることが望ましいと考えられる。 Under these conditions, when focusing on the quality characteristics at the time of production, if the amount of refined white sugar per vial is large or the white sugar concentration of the filling solution is high, the proportion of appearance defects at the time of production is high Also tended to be higher. It is considered that water removal in the lyophilization process did not proceed normally in these lyophilizates. The water removal in the lyophilization process proceeds as the frozen moisture sublimes and is released from the upper surface of the lyophilizate, so the amount of sucrose per area of the upper surface of the lyophilizate (internal cross-sectional area of the container) decreases Water removal efficiency is considered to be high. Also in this examination, in the same size vial, the smaller the amount of sucrose and the lower the concentration of sucrose, the lower the moisture content at the time of production tends to be. Therefore, in order to ensure good formulation quality characteristics at the time of manufacture, it is necessary to reduce the amount of refined white sugar per internal cross-sectional area of the container (usually about 1.85 mg / mm 2 or less). Also, for the same purpose, the concentration of the filling solution used for lyophilization is about 140 mg / mL or less, considering that the quality characteristics in the case of Formulation Example 4 (160 mg / mL) slightly did not reach the standard. It is considered desirable to be there.
また、熱苛酷保管後において良好な品質特性を確保するためには、製造時の含有水分が少ないことが重要であるが、製造時の水分含量が十分に低い場合であっても、バイアル当たりの白糖量が少なすぎる場合には、ゴム栓等に含まれる水分を保管中に凍結乾燥体が吸収してしまうことの影響が無視できず、保管後の水分含量が規定値以上となってしまうことが示唆された。ゴム栓のサイズは、バイアル径に比例して大きくなることから、ゴム栓の水分の影響を考える場合にも容器の内部断面積当たりの白糖量として考える必要があり、内部断面積当たり約0.50mg/mm2以上とする必要があるものと考えられる。 Also, in order to ensure good quality characteristics after heat and severe storage, it is important that the water content at the time of manufacture be small, but even if the water content at the time of manufacture is sufficiently low, per vial If the amount of white sugar is too small, the influence of the absorption of the freeze-dried product during storage can not be ignored during storage, and the water content after storage will be above the specified value Was suggested. Since the size of the rubber stopper increases in proportion to the diameter of the vial, it is necessary to consider it as the amount of sucrose per internal cross sectional area of the container even when considering the effect of the water content of the rubber stopper. It is considered that it is necessary to be 50 mg / mm 2 or more.
<実施例2:実薬製剤の製造及び評価>
実施例1で好ましいと判断された白糖配合条件(内径22.1mmのバイアル1本につき300〜500 mg)、白糖濃度(125 mg/mL以下)によりカルペリチド含有製剤(カルペリチド1mg含有)を製造し、製造時の特性、及び、熱安定性を評価した。
(1)配合例A(カルペリチド1 mg/バイアル、白糖量500 mg/バイアル(1.30mg/mm2)、白糖濃度100mg/mL(10%))の凍結乾燥製剤の製造
カルペリチド 81.6 mg(カルペリチドの設計含量1mg設計に対し、2%の増仕込み)及び精製白糖(日本薬局方、塩水港精糖株式会社)40 gを精製水に溶解した後、精製水で全量を400mLとした。この溶液をフィルター(Stericup-GV 0.22μm、PVDF、Millipore Corporation)にて濾過した後、テーハー分注機(FH-10s、株式会社ヒラサワ)またはマイクロスケールピペット(PIPETMAN、GILSON, Inc.など)を用い、5 mLをガラスバイアル(胴外径24.5 mm、内径22.1 mm)、大和特殊硝子株式会社)に充填した。充填済バイアルに、ゴム栓(V10-F8 D713 RB2-40、株式会社大協精工)を半打栓した後、凍結乾燥機(RL-30KPs、共和真空株式会社)に搬入し、予備凍結(−50℃設定)、引き続いて真空条件下(20 Pa設定)で凍結乾燥(一次乾燥:−20〜−5℃設定、二次乾燥:40℃設定)を行い、乾燥終了後にバイアル内を窒素導入により復圧した。バイアルにゴム栓を全打栓した後、巻締機(GAC-01、株式会社稲葉機械製作所)を用いてフリップオフキャップ(APキャップ、20AP7.0H、石田プレス工業株式会社)でバイアルを巻き締めし、配合例Aのカルペリチド含有製剤を得た。
Example 2 Production and Evaluation of Active Preparations
A carperitide-containing preparation (containing 1 mg of carperitide) was prepared under the sucrose mixing conditions (300 to 500 mg per vial with an inner diameter of 22.1 mm) judged to be preferable in Example 1 and the sucrose concentration (125 mg / mL or less) The characteristics at the time of production and the thermal stability were evaluated.
(1) Preparation of a lyophilized preparation of Formulation Example A (carperitide 1 mg / vial, sucrose amount 500 mg / vial (1.30 mg / mm 2 ), sucrose concentration 100 mg / mL (10%)) Carperitide 81.6 mg ( After 1% of design content of carperitide was designed, 2 g of additional preparation and 40 g of purified white sugar (Japanese Pharmacopoeia, Saltwater Port Sugar Co., Ltd.) were dissolved in purified water, and then the total volume was adjusted to 400 mL with purified water. This solution is filtered through a filter (Stericup-GV 0.22 μm, PVDF, Millipore Corporation), and then a Tehha dispenser (FH-10s, Hirasawa Co., Ltd.) or a microscale pipette (PIPETMAN, GILSON, Inc., etc.) is used. 5 mL was filled in a glass vial (body outer diameter 24.5 mm, inner diameter 22.1 mm) (Daiwa Special Glass Co., Ltd.). After half-stopping a rubber stopper (V10-F8 D713 RB2-40, Daikyo Seiko Co., Ltd.) into the filled vial, it is carried into a lyophilizer (RL-30 KPs, Kyowa Vacuum Co., Ltd.) and pre-frozen (- (50 ° C setting), followed by lyophilization (primary drying: -20 to -5 ° C setting, secondary drying: 40 ° C setting) under vacuum conditions (20 Pa setting), and after the end of drying, the vial is filled with nitrogen It pressured again. After all the rubber stoppers have been plugged into the vial, use a clamping machine (GAC-01, Inaba Machine Mfg. Co., Ltd.) to clamp the vial with a flip-off cap (AP cap, 20AP7.0H, Ishida Press Co., Ltd.) To obtain a carperitide-containing preparation of Formulation Example A.
(2)配合例B(カルペリチド1 mg/バイアル、白糖量300 mg/バイアル(0.78 mg/mm2)、白糖濃度75 mg/mL(7.5%))の凍結乾燥製剤の製造
カルペリチド 102 mg(カルペリチドの設計含量1mg設計に対し、2%の増仕込み)及び精製白糖(日本薬局方、塩水港精糖株式会社)30 gを精製水に溶解した後、精製水で全量を400mLとした。この溶液をフィルター(Stericup-GV 0.22μm、PVDF、Millipore Corporation)にて濾過した後、テーハー分注機(FH-10s、株式会社ヒラサワ)またはマイクロスケールピペット(PIPETMAN、GILSON, Inc.など)を用い、4 mLをガラスバイアル(胴外径24.5 mm、内径22.1 mm)、大和特殊硝子株式会社)に充填した。以下、配合例Aと同じ方法により、配合例Bのカルペリチド含有製剤を得た。
(2) Preparation of a lyophilized preparation of combination example B (carperitide 1 mg / vial, sucrose amount 300 mg / vial (0.78 mg / mm 2 ), sucrose concentration 75 mg / mL (7.5%)) Carperitide 102 mg (supplemented addition of 2% to the design content of 1 mg of carperitide) and 30 g of purified white sugar (Japanese Pharmacopoeia, Saltwater Port Semi-sugar Co., Ltd.) were dissolved in purified water, and then the total volume was made 400 mL with purified water. This solution is filtered through a filter (Stericup-GV 0.22 μm, PVDF, Millipore Corporation), and then a Tehha dispenser (FH-10s, Hirasawa Co., Ltd.) or a microscale pipette (PIPETMAN, GILSON, Inc., etc.) is used. Then, 4 mL was filled in a glass vial (body outer diameter 24.5 mm, inner diameter 22.1 mm) (Daiwa Special Glass Co., Ltd.). Thereafter, the carperitide-containing preparation of Formulation Example B was obtained by the same method as in Formulation Example A.
(3)カルペリチド含有製剤の熱苛酷保存安定性の評価
配合例A及びBの製剤を40℃75%RHに設定した恒温恒湿槽(LH31-15M型、株式会社ナガノ科学機械製作所)で1ヶ月間もしくは3ヶ月間、または、50℃に設定した恒温槽(CH-P 30-01型、株式会社ナガノ科学機械製作所)で1ヶ月間保管した。これらの製剤について、製造時、各保管前及び保管後に、実施例1と同様の基準で目視による外観判定(製造時:9本、保管後:3本)を行った。また、保管後の製剤について、以下の方法でカルペリチド及び類縁物質の含有量を測定した。
(3) Evaluation of heat and severe storage stability of carperitide-containing preparation One month in a constant temperature and humidity chamber (LH 31-15 M type, Nanono Scientific Machine Co., Ltd.) with the preparation of Formulation Examples A and B set at 40 ° C and 75% RH. It was stored for 1 month in a constant temperature bath (CH-P 30-01 type, Nanono Scientific Machinery Co., Ltd.) set at 50 ° C. for 3 months. With respect to these preparations, visual appearance determination (at the time of production: nine, after storage: three) was performed according to the same standard as in Example 1 at the time of manufacture, before and after each storage. In addition, for the preparation after storage, the content of carperitide and related substances was measured by the following method.
[方法:製剤中のカルペリチド含量及び類縁物質の測定]
製剤1本につき、希酢酸を添加して内容物を溶解してから全量を10 mLとし、試料溶液とした。また、この試料溶液を希酢酸で20倍に希釈し、類縁物質用標準溶液とした。カルペリチド定量用標準溶液は、別途調製したものを用いた。
高速液体クロマトグラフ装置(株式会社島津製作所)により、固定相にODSカラム、移動相に水/アセトニトルを用いる逆相分離系で、試料溶液、カルペリチド定量用標準溶液、類縁物質試験用標準溶液を測定した(測定本数:3本)。
含量は次のように算出した。高速液体クロマトグラフ法(検出:紫外吸光度法)による試料溶液、カルペリチド定量用標準溶液の測定結果から、1バイアル当りのカルペリチド量を算出し、カルペリチドの設計含量(1mg)に対する比率を求め、これをカルペリチド含量(%)とした。
類縁物質は次のように算出した。高速液体クロマトグラフ法(紫外吸光度検出)による試料溶液、類縁物質用標準溶液の測定結果から、試料溶液の類縁物質ピークエリアの、類縁物質用標準溶液のカルペリチドピークエリアの20倍値に対する比を求め、これを類縁物質量(%)とした。
[Method: Measurement of Carperitide Content and Related Substances in Preparation]
Diluted acetic acid was added to one preparation to dissolve the contents, and then the total volume was adjusted to 10 mL to obtain a sample solution. In addition, this sample solution was diluted 20 times with dilute acetic acid to prepare a standard solution for related substances. As a standard solution for determination of carperitide, one prepared separately was used.
Measure sample solution, standard solution for determination of carperitide, standard solution for related substance test with reversed phase separation system using ODS column as stationary phase and water / acetonitrile as mobile phase by high performance liquid chromatograph (Shimadzu Corporation) (Number of measurements: 3).
The content was calculated as follows. The amount of carperitide per vial is calculated from the measurement results of the sample solution and standard solution for determination of carperitide by high performance liquid chromatography (detection: ultraviolet absorbance method), and the ratio to the design content of carperitide (1 mg) is determined Carperitide content (%).
The related substances were calculated as follows. From the measurement results of the sample solution and the standard solution for relative substances by high performance liquid chromatography (ultraviolet absorbance detection), the ratio of the peak area of the analog substance of the sample solution to the 20 times value of the peak area of This was regarded as the related substance mass (%).
[結果:カルペリチド含有製剤の製剤特性と熱安定性]
配合例AおよびBの製剤の製造時の外観形状、並びに、40℃75%RH1ヶ月および3ヶ月保管時、50℃1ヶ月保管時の外観形状及び含有成分の評価結果を表4に示した。
配合例A(白糖量:500 mg/バイアル、1.30mg/mm2、白糖濃度:100 mg/mL)、及び、配合例B(白糖量:300 mg/バイアル:0.78mg/mm2、白糖濃度:75 mg/mL)のカルペリチド含有製剤は、いずれも製造時、40℃75%RH3ヶ月、50℃1ヶ月の熱苛酷期間を通じ、外観形状は正常形状から変化なく良好に維持されていることが明らかである。また、これらの熱苛酷保管期間においてカルペリチド含量の低下、及び、類縁物質の増加はほとんど認められず、主薬の化学的安定性も極めて良好であることがわかる。また、配合例A、Bと同様の精製白糖配合条件で別途同様の試験を行い、製造時、熱苛酷保管時の含水率はいずれも0.5%以下であった。以上のことから、これらの配合条件で作製した凍結乾燥製剤は室温保存を貯法とする製剤に適した品質特性を有することが示された。
[Result: Formulation characteristics and thermal stability of carperitide-containing preparation]
Table 4 shows the appearances of the preparations of Formulation Examples A and B at the time of production, and the evaluation results of the appearances and the ingredients after storage at 40 ° C., 75% RH for 1 month and 3 months, and at 50 ° C. for 1 month.
Formulation Example A (amount of sucrose: 500 mg / vial, 1.30 mg / mm 2 , concentration of sucrose: 100 mg / mL), and Example B (amount of sucrose: 300 mg / vial: 0.78 mg / mm 2 , sucrose) Each of the carperitide-containing preparations with a concentration of 75 mg / mL) maintained their external shape well from the normal shape during the heat stress period of 3 months at 40 ° C 75% RH and 1 month at 50 ° C. Is clear. In addition, it can be seen that the decrease in carperitide content and the increase in related substances are hardly observed during these heat and severe storage periods, and the chemical stability of the main drug is also extremely good. Further, the same tests were conducted separately under the same conditions for blending refined sucrose as in Formulation Examples A and B, and the moisture content at the time of heat stress storage was 0.5% or less at the time of production. From the above, it was shown that the lyophilized formulations prepared under these combination conditions have quality characteristics suitable for formulations stored at room temperature.
※:実測値(製剤3本の判定符号)を記載.
※: Actual measurement value (determination code of 3 preparations) is indicated.
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