JP6884496B1 - Injectable preparation containing levetiracetam as an active ingredient - Google Patents
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- HPHUVLMMVZITSG-ZCFIWIBFSA-N levetiracetam Chemical compound CC[C@H](C(N)=O)N1CCCC1=O HPHUVLMMVZITSG-ZCFIWIBFSA-N 0.000 title claims abstract description 57
- 229960004002 levetiracetam Drugs 0.000 title claims abstract description 56
- 238000002360 preparation method Methods 0.000 title claims abstract description 33
- 239000004480 active ingredient Substances 0.000 title description 2
- 230000001954 sterilising effect Effects 0.000 claims abstract description 27
- 238000004659 sterilization and disinfection Methods 0.000 claims abstract description 22
- FAPWRFPIFSIZLT-UHFFFAOYSA-M Sodium chloride Chemical compound [Na+].[Cl-] FAPWRFPIFSIZLT-UHFFFAOYSA-M 0.000 claims abstract description 20
- 238000011049 filling Methods 0.000 claims abstract description 20
- 238000004519 manufacturing process Methods 0.000 claims abstract description 12
- VMHLLURERBWHNL-UHFFFAOYSA-M Sodium acetate Chemical compound [Na+].CC([O-])=O VMHLLURERBWHNL-UHFFFAOYSA-M 0.000 claims abstract description 10
- 239000001632 sodium acetate Substances 0.000 claims abstract description 10
- 235000017281 sodium acetate Nutrition 0.000 claims abstract description 10
- 239000011780 sodium chloride Substances 0.000 claims abstract description 10
- 239000000243 solution Substances 0.000 claims description 23
- 238000001914 filtration Methods 0.000 claims description 22
- 238000002347 injection Methods 0.000 claims description 16
- 239000007924 injection Substances 0.000 claims description 16
- 238000002156 mixing Methods 0.000 claims description 8
- 238000010438 heat treatment Methods 0.000 claims description 3
- 239000011148 porous material Substances 0.000 claims description 3
- 238000004090 dissolution Methods 0.000 claims description 2
- 239000010419 fine particle Substances 0.000 abstract description 14
- 238000010586 diagram Methods 0.000 abstract 1
- 239000007972 injectable composition Substances 0.000 abstract 1
- QTBSBXVTEAMEQO-UHFFFAOYSA-N Acetic acid Chemical compound CC(O)=O QTBSBXVTEAMEQO-UHFFFAOYSA-N 0.000 description 20
- 229940090044 injection Drugs 0.000 description 9
- 238000004811 liquid chromatography Methods 0.000 description 9
- 238000000034 method Methods 0.000 description 9
- 229960000583 acetic acid Drugs 0.000 description 7
- 239000000047 product Substances 0.000 description 7
- 206010010904 Convulsion Diseases 0.000 description 5
- 239000012467 final product Substances 0.000 description 5
- 239000000203 mixture Substances 0.000 description 5
- 101710084141 Synaptic vesicle glycoprotein 2A Proteins 0.000 description 4
- 239000008186 active pharmaceutical agent Substances 0.000 description 4
- 229940088679 drug related substance Drugs 0.000 description 4
- 238000005259 measurement Methods 0.000 description 4
- 239000008213 purified water Substances 0.000 description 4
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Chemical compound O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 4
- WEVYAHXRMPXWCK-UHFFFAOYSA-N Acetonitrile Chemical compound CC#N WEVYAHXRMPXWCK-UHFFFAOYSA-N 0.000 description 3
- 239000002552 dosage form Substances 0.000 description 3
- 230000000694 effects Effects 0.000 description 3
- 238000009472 formulation Methods 0.000 description 3
- 239000011550 stock solution Substances 0.000 description 3
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 description 2
- FEWJPZIEWOKRBE-JCYAYHJZSA-N Dextrotartaric acid Chemical compound OC(=O)[C@H](O)[C@@H](O)C(O)=O FEWJPZIEWOKRBE-JCYAYHJZSA-N 0.000 description 2
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 2
- FEWJPZIEWOKRBE-UHFFFAOYSA-N Tartaric acid Natural products [H+].[H+].[O-]C(=O)C(O)C(O)C([O-])=O FEWJPZIEWOKRBE-UHFFFAOYSA-N 0.000 description 2
- 239000004809 Teflon Substances 0.000 description 2
- 229920006362 Teflon® Polymers 0.000 description 2
- 238000013329 compounding Methods 0.000 description 2
- 239000003814 drug Substances 0.000 description 2
- 239000000706 filtrate Substances 0.000 description 2
- 230000005764 inhibitory process Effects 0.000 description 2
- 229940102223 injectable solution Drugs 0.000 description 2
- 239000002994 raw material Substances 0.000 description 2
- 238000007789 sealing Methods 0.000 description 2
- 238000003756 stirring Methods 0.000 description 2
- 230000001629 suppression Effects 0.000 description 2
- 235000002906 tartaric acid Nutrition 0.000 description 2
- 239000011975 tartaric acid Substances 0.000 description 2
- 239000002699 waste material Substances 0.000 description 2
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 1
- 102000004310 Ion Channels Human genes 0.000 description 1
- 208000037158 Partial Epilepsies Diseases 0.000 description 1
- 206010061334 Partial seizures Diseases 0.000 description 1
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 1
- 206010053648 Vascular occlusion Diseases 0.000 description 1
- 239000013543 active substance Substances 0.000 description 1
- 230000008850 allosteric inhibition Effects 0.000 description 1
- 229910021529 ammonia Inorganic materials 0.000 description 1
- 239000001961 anticonvulsive agent Substances 0.000 description 1
- 229960003965 antiepileptics Drugs 0.000 description 1
- 239000007864 aqueous solution Substances 0.000 description 1
- ULEAQRIQMIQDPJ-UHFFFAOYSA-N butane-1,2-diamine Chemical compound CCC(N)CN ULEAQRIQMIQDPJ-UHFFFAOYSA-N 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 239000003153 chemical reaction reagent Substances 0.000 description 1
- 238000004440 column chromatography Methods 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 229940079593 drug Drugs 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 206010015037 epilepsy Diseases 0.000 description 1
- 238000011705 epilepsy animal model Methods 0.000 description 1
- 125000001495 ethyl group Chemical group [H]C([H])([H])C([H])([H])* 0.000 description 1
- 201000007186 focal epilepsy Diseases 0.000 description 1
- 229960003692 gamma aminobutyric acid Drugs 0.000 description 1
- BTCSSZJGUNDROE-UHFFFAOYSA-N gamma-aminobutyric acid Chemical compound NCCCC(O)=O BTCSSZJGUNDROE-UHFFFAOYSA-N 0.000 description 1
- 239000012362 glacial acetic acid Substances 0.000 description 1
- 230000000575 glycinergic effect Effects 0.000 description 1
- 230000001771 impaired effect Effects 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- 238000001802 infusion Methods 0.000 description 1
- 230000003834 intracellular effect Effects 0.000 description 1
- 238000001990 intravenous administration Methods 0.000 description 1
- 238000010930 lactamization Methods 0.000 description 1
- 229940037125 levetiracetam injection Drugs 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 238000000691 measurement method Methods 0.000 description 1
- 239000011259 mixed solution Substances 0.000 description 1
- 238000012544 monitoring process Methods 0.000 description 1
- 230000001537 neural effect Effects 0.000 description 1
- 210000002569 neuron Anatomy 0.000 description 1
- 230000003472 neutralizing effect Effects 0.000 description 1
- 230000003287 optical effect Effects 0.000 description 1
- 239000006186 oral dosage form Substances 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 239000000825 pharmaceutical preparation Substances 0.000 description 1
- 229940127557 pharmaceutical product Drugs 0.000 description 1
- 238000011085 pressure filtration Methods 0.000 description 1
- 125000001436 propyl group Chemical group [H]C([*])([H])C([H])([H])C([H])([H])[H] 0.000 description 1
- HNJBEVLQSNELDL-UHFFFAOYSA-N pyrrolidin-2-one Chemical group O=C1CCCN1 HNJBEVLQSNELDL-UHFFFAOYSA-N 0.000 description 1
- 238000011002 quantification Methods 0.000 description 1
- 238000011160 research Methods 0.000 description 1
- 150000003839 salts Chemical class 0.000 description 1
- 239000000741 silica gel Substances 0.000 description 1
- 229910002027 silica gel Inorganic materials 0.000 description 1
- 229910001220 stainless steel Inorganic materials 0.000 description 1
- 239000010935 stainless steel Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 238000010998 test method Methods 0.000 description 1
- 208000021331 vascular occlusion disease Diseases 0.000 description 1
- 238000005303 weighing Methods 0.000 description 1
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- Medicinal Preparation (AREA)
- Pharmaceuticals Containing Other Organic And Inorganic Compounds (AREA)
Abstract
【課題】容器充填および加熱滅菌後に生じる不溶性微粒子の少ない製剤の提供および前記製剤の製造方法の提供。【解決手段】レベチラセタム、塩化ナトリウム及び酢酸ナトリウムを含む注射用製剤であって、pHが5.53〜5.66であり、前記注射用製剤中のレベチラセタムの量が、配合量の99.7〜100.4%である、注射用製剤。【選択図】なしPROBLEM TO BE SOLVED: To provide a preparation having a small amount of insoluble fine particles generated after container filling and heat sterilization, and to provide a method for producing the above-mentioned preparation. SOLUTION: This is an injectable preparation containing levetiracetam, sodium chloride and sodium acetate, the pH is 5.53 to 5.66, and the amount of levetiracetam in the injectable preparation is 99.7 to 99.7 to the blended amount. An injectable formulation that is 100.4%. [Selection diagram] None
Description
本発明はレベチラセタムを有効成分とする注射用製剤に関する。 The present invention relates to an injectable preparation containing levetiracetam as an active ingredient.
レベチラセタム((2S)-2-(2-Oxopyrrolidine-1-yl)butyramide)は、2−オキソ−1−ピロリジン骨格を有し、その構造に不斉炭素を1個有するS−エナンチオマーである。本邦において、レベチラセタムは、抗てんかん薬(イーケプラ(登録商標)点滴静注500mg等)として販売されており、てんかん患者の部分発作(二次性全般化発作を含む)の治療等に用いられている。レベチラセタムは、各種受容体及び主要なイオンチャネルとは結合しないが、神経終末のシナプス小胞タンパク質2A(SV2A)との結合、N型Ca2+チャネル阻害、細胞内のCa2+遊離抑制、GABA及びグリシン作動性電流に対するアロステリック阻害の抑制、神経細胞間の過剰な同期化の抑制などが確認されている。SV2Aに対する結合親和性と各種てんかん動物モデルにおける発作抑制作用との間には相関が認められることから、レベチラセタムとSV2Aの結合が、発作抑制作用に寄与しているものと考えられている(例えば、非特許文献1を参照)。 Levetiracetam ((2S) -2- (2-Oxopyrrolidine-1-yl) butyramide) is an S-enantiomer having a 2-oxo-1-pyrrolidin skeleton and one asymmetric carbon in its structure. In Japan, levetiracetam is marketed as an antiepileptic drug (Ekepla (registered trademark) intravenous drip infusion 500 mg, etc.) and is used for the treatment of partial epilepsy (including secondary generalized seizures) in epilepsy patients. .. Levetiracetam does not bind to various receptors and major ion channels, but binds to synaptic vesicle protein 2A (SV2A) at neuronal terminals, N-type Ca2 + channel inhibition, intracellular Ca2 + release inhibition, GABA and glycinergic. Suppression of allosteric inhibition of current and suppression of excessive synchronization between nerve cells have been confirmed. Since there is a correlation between the binding affinity for SV2A and the seizure-suppressing effect in various epilepsy animal models, it is considered that the binding between levetiracetam and SV2A contributes to the seizure-suppressing effect (for example,). See Non-Patent Document 1).
レベチラスタムの製造方法については、2-アミノブチルアミドを製造し、これを光学活性な酒石酸を用いてジアステレオマーとして分離し、酒石酸を除去し、光学活性なエチル(S)-4-{[1-アミノカルボニル]プロピル}アミノブチレート塩酸塩となし、これを中和し、ラクタム化してレベチラセタムに変換する方法が知られている(例えば、特許文献1を参照)。
また、レベチラセタムは、試薬としてもシグマ・アルドリッチ社より販売もされている。
また、近年においては、レベチラセタムの誘導体において、ピロリドン骨格に、エチル−2−ブロモブチラーを縮合させ、アンモニア分解を行い、相当するラセミ体を得、これを光学分割カラムクロマトグラフィーで光学活性体に分割する技術も開発されている(例えば、特許文献2を参照)。レベチラセタムは、この技術を応用して得ることもできる。
Regarding the method for producing levetylastam, 2-aminobutylamide is produced, which is separated as a diastereomer using optically active tartaric acid, tartaric acid is removed, and optically active ethyl (S) -4-{[1. -Aminocarbonyl] propyl} aminobutyrate hydrochloride is known, and a method of neutralizing this and converting it to lactamization to levetylacetam is known (see, for example, Patent Document 1).
Levetiracetam is also sold as a reagent by Sigma-Aldrich.
Further, in recent years, in a derivative of levetiracetam, ethyl-2-bromobutyral is condensed with a pyrrolidone skeleton and decomposed with ammonia to obtain a corresponding racemate, which is divided into optically active substances by optical resolution column chromatography. Techniques have also been developed (see, eg, Patent Document 2). Levetiracetam can also be obtained by applying this technology.
現在上市されているレベチラセタムの剤形は、経口投与剤形と注射剤形の2種であるが、てんかん発作時に素早く発作を止める必要があることから、効果発現の素早い注射剤形はてんかん発作治療において、重要な位置づけにある。レベチラセタム注射剤形は、pHを5.0〜6.0に調整されている(https://www.info.pmda.go.jp/go/pack/1139010F1024_1_22/を参照)が、これは、2−オキソ−1−ピロリジン骨格の化合物の水性溶液がこの範囲内において安定に存在するためである(例えば、特許文献2を参照)。
しかしながら、この注射剤形の製品の生産においては、容器に充填前の溶液が製品規格値内であっても、容器に充填し、加熱滅菌した後、出荷判定を行った際に不溶性微細粒子の発生により、ロットアウトしてしまい、廃棄せざるを得ない場合があった。このような不溶性微細粒子は、注射薬においては血管閉塞などの原因ともなりかねないため、医薬品医療機器総合機構(PMDA)の審査においても厳しく管理されており、この基準をクリア出来ない製品は廃棄せざるを得ない。このため、当該基準をクリアし、供給の安定性を確保する手段が求められていた。不溶性微粒子の発生原因については、詳細は不明であるが、原体の規格値に現れない極微量の不純物の塩などによるものではないかと推測される。
There are two dosage forms of levetiracetam currently on the market, an oral dosage form and an injectable dosage form, but since it is necessary to stop the attack quickly at the time of a seizure attack, the injectable dosage form with rapid onset of effect is a treatment for seizure. In, it is in an important position. The levetiracetam injectable form has a pH adjusted to 5.0-6.0 (see https://www.info.pmda.go.jp/go/pack/1139010F1024_1_22/), which is 2 This is because an aqueous solution of a compound having a −oxo-1-pyrrolidin skeleton exists stably within this range (see, for example, Patent Document 2).
However, in the production of this injection-type product, even if the solution before filling in the container is within the product standard value, insoluble fine particles are found when the container is filled, sterilized by heating, and then the shipment is judged. Due to the occurrence, the lot was out and there was a case where it had to be discarded. Since such insoluble fine particles may cause vascular occlusion in injectable drugs, they are strictly controlled by the Pharmaceuticals and Medical Devices Agency (PMDA), and products that cannot meet this standard are discarded. I have no choice but to do it. Therefore, there has been a demand for a means for clearing the standard and ensuring the stability of supply. The cause of the generation of insoluble fine particles is unknown, but it is presumed that it is due to a very small amount of impurities such as salts that do not appear in the standard values of the drug substance.
このような背景下、容器充填、加熱滅菌後に生じた不溶性微粒子によるロットアウトを防ぎ、製品の廃棄量を減らす方法が求められていた。 Against this background, there has been a demand for a method of reducing the amount of product waste by preventing lot-out due to insoluble fine particles generated after container filling and heat sterilization.
このような状況に鑑みて、本発明者らは、容器充填、加熱滅菌後に生じた不溶性微粒子によるロットアウトを防ぐ方策を求めて、鋭意研究、努力を重ねた結果、容器に充填する前の液剤のpHを5.66〜5.53に、かつ、レベチラセタムの量が、配合量の99.7〜100.4%となるように調整すると、ロットアウトが確実に防止し得ることを見いだし、発明を完成させるに至った。すなわち、本発明は以下に示すとおりである。
<1>
レベチラセタム、塩化ナトリウム及び酢酸ナトリウムを含む注射用製剤であって、
pHが5.53〜5.66であり、
前記注射用製剤中のレベチラセタムの量が、配合量の99.7〜100.4%である、注射用製剤。
<2>
滅菌濾過製剤である、<1>に記載の注射用製剤。
<3>
前記レベチラセタムの配合量が、10%(w/v)である、<1>または<2>に記載の注射用製剤。
<4>
(a)レベチラセタム、塩化ナトリウム及び酢酸ナトリウムを配合する工程と、
(b)工程(a)で得られた溶液を滅菌濾過する工程とを含む、注射用製剤の製造方法であって、
工程(b)の滅菌濾過を経て得られた充填前溶液中のレベチラセタムの量が、工程(a)におけるレベチラセタムの配合量の99.7〜100.4%であり、かつ前記溶液のpHが5.53〜5.66であることを特徴とする、注射用製剤の製造方法。
<5>
(c)工程(b)の滅菌濾過を経て得られた充填前溶液を容器に充填し、加熱滅菌する工程をさらに含む、<4>に記載の製造方法。
In view of this situation, the present inventors have sought measures to prevent lot-out due to insoluble fine particles generated after container filling and heat sterilization, and as a result of diligent research and efforts, the liquid preparation before filling in the container. The invention was found to be able to reliably prevent lot-out by adjusting the pH of the above to 5.66 to 5.53 and the amount of levetiracetam to be 99.7 to 100.4% of the compounding amount. Has been completed. That is, the present invention is as shown below.
<1>
An injectable preparation containing levetiracetam, sodium chloride and sodium acetate.
The pH is 5.53 to 5.66 and
An injectable preparation in which the amount of levetiracetam in the injectable preparation is 99.7 to 100.4% of the blended amount.
<2>
The injectable preparation according to <1>, which is a sterilized filtration preparation.
<3>
The injectable preparation according to <1> or <2>, wherein the blending amount of levetiracetam is 10% (w / v).
<4>
(A) Step of blending levetiracetam, sodium chloride and sodium acetate, and
(B) A method for producing an injectable preparation, which comprises a step of sterilizing and filtering the solution obtained in step (a).
The amount of levetiracetam in the prefill solution obtained through the sterilization filtration in the step (b) is 99.7 to 100.4% of the blended amount of levetiracetam in the step (a), and the pH of the solution is 5. A method for producing an injectable preparation, which comprises .53 to 5.66.
<5>
(C) The production method according to <4>, further comprising a step of filling a container with the pre-filling solution obtained through the sterilization filtration of the step (b) and sterilizing by heating.
本願明細書において、レベチラセタムの「配合量」とは、製剤の原料配合時におけるレベチラセタムの重量である。また、「定量値」とは、製剤を容器に充填する前の溶液(充填前溶液)におけるレベチラセタムの重量であり、液体クロマトグラフィーにより測定した、レベチラセタムのピーク面積と、レベチラセタムの標準物質のピーク面積の比より算出した重量を意味する。なお、この定量値は、容器に充填した後の製剤についての値と同じである。 In the specification of the present application, the "blending amount" of levetiracetam is the weight of levetiracetam at the time of blending the raw materials of the preparation. The "quantitative value" is the weight of levetiracetam in the solution before filling the container (solution before filling), and the peak area of levetiracetam and the peak area of the standard substance of levetiracetam measured by liquid chromatography. It means the weight calculated from the ratio of. In addition, this quantitative value is the same as the value for the pharmaceutical product after filling in a container.
本発明によれば、レベチラセタム注射用製剤において、容器充填、加熱滅菌後に生じた不溶性微粒子によるロットアウトを事前に防ぎ、製品の廃棄量を確実に減らすことができる。このため、レベチラセタム注射用製剤の製造における経済性を格段に向上させることができる。 According to the present invention, in the levetiracetam injection preparation, lot-out due to insoluble fine particles generated after container filling and heat sterilization can be prevented in advance, and the amount of product waste can be reliably reduced. Therefore, the economic efficiency in the production of the levetiracetam injectable preparation can be remarkably improved.
本発明は、容器充填および加熱滅菌後に生じる不溶性微粒子の少ない製剤の提供および当該製剤の製造方法の提供に関する。
本発明に係る注射用製剤は、レベチラセタム、塩化ナトリウム及び酢酸ナトリウムを含有する。本発明に係る注射用製剤は、レベチラセタムと、塩化ナトリウムと、酢酸ナトリウムを配合し、酢酸によりpHを調整し、滅菌濾過することにより製造することができる。さらに、滅菌濾過したレベチラセタムの注射剤用溶液を、容器に充填し、密閉した後、加熱滅菌してもよい。酢酸の添加により調整されるpHの範囲は、5.3〜5.7である。これは、最終製品において、レベチラセタムが安定なpH域5〜6を実現するための、安全域を見込んだ範囲である。酢酸は、氷酢酸を用いてもよい。
The present invention relates to the provision of a preparation having a small amount of insoluble fine particles generated after container filling and heat sterilization, and the provision of a method for producing the preparation.
The injectable preparation according to the present invention contains levetiracetam, sodium chloride and sodium acetate. The injectable preparation according to the present invention can be produced by blending levetiracetam, sodium chloride and sodium acetate, adjusting the pH with acetic acid, and sterilizing and filtering. Further, a sterilized and filtered solution for injection of levetiracetam may be filled in a container, sealed, and then heat sterilized. The pH range adjusted by the addition of acetic acid is 5.3 to 5.7. This is a safe range for levetiracetam to achieve a stable pH range of 5 to 6 in the final product. As acetic acid, glacial acetic acid may be used.
本発明に係る注射用製剤に含まれる塩化ナトリウムの含有量は、好ましくは0.85〜0.95%(w/v)であり、より好ましくは0.90%(w/v)(±0.01%)である。また、本発明に係る注射用製剤に含まれる酢酸ナトリウムの含有量は、好ましくは0.16〜0.17%(w/v)であり、より好ましくは0.164%(w/v)(±0.002%)である。 The content of sodium chloride contained in the injectable preparation according to the present invention is preferably 0.85 to 0.95% (w / v), more preferably 0.90% (w / v) (± 0). 0.01%). The content of sodium acetate contained in the injectable preparation according to the present invention is preferably 0.16 to 0.17% (w / v), more preferably 0.164% (w / v) ( ± 0.002%).
前記注射剤用の溶液は、次に示す工程によって製造される。 The solution for injection is produced by the following steps.
<レベチラセタムの注射剤用溶液の作製工程>
工程(a):配合工程
原料となるレベチラセタム原薬、塩化ナトリウム及び酢酸ナトリウムに対し、注射用の精製水を加え、攪拌、溶解する。レベチラセタム原薬、塩化ナトリウム及び酢酸ナトリウムの量は、それぞれ、最終製品濃度が、10%(w/v)、0.85〜0.95%(w/v)、0.16〜0.17%(w/v)になるように調整する。pHの前調整用に、配合時に少量の酢酸を加えてもよい。配合されるレベチラセタム原薬は、表1に示す規格値のものが好ましく用いられる。溶解後、pHを測定し、pHが5.3〜5.7(最終製品濃度)の範囲に入るように調整しながら、酢酸を加える。酢酸添加後、最終重量が所定量になるように、精製水をさらに加える。上記最終濃度は、本発明に係る注射用製剤における濃度を意味する。
工程(a)はコンベンショナルな条件で行うことができる。
<Preparation process of levetiracetam injectable solution>
Step (a): Blending step Purified water for injection is added to the levetiracetam drug substance, sodium chloride and sodium acetate as raw materials, and the mixture is stirred and dissolved. The final product concentrations of levetiracetam drug substance, sodium chloride and sodium acetate were 10% (w / v), 0.85 to 0.95% (w / v), and 0.16 to 0.17%, respectively. Adjust so that it becomes (w / v). A small amount of acetic acid may be added at the time of formulation for pH pre-adjustment. As the levetiracetam drug substance to be blended, those having standard values shown in Table 1 are preferably used. After dissolution, the pH is measured and acetic acid is added while adjusting the pH to be in the range of 5.3 to 5.7 (final product concentration). After the addition of acetic acid, more purified water is added so that the final weight becomes a predetermined amount. The final concentration means the concentration in the injectable preparation according to the present invention.
Step (a) can be performed under conventional conditions.
工程(b):滅菌濾過工程
前記工程(a)で得られた溶液を滅菌濾過する。滅菌濾過は1回または2回以上実施することができるが、2回以上が好ましい。2回の滅菌濾過を実施する場合、例えば、第一次滅菌濾過の濾液から、次の第二次滅菌濾過の為の容器は無菌管理し、第一次滅菌濾過以後、容器に充填、密封までの工程は無菌状態で行うことができる。滅菌濾過は、ポアサイズが0.2μm〜0.4μm、好ましくは0.2μmのテフロンフィルターを用いて、加圧濾過にて行う。
<充填前溶液の測定>
前記滅菌濾過を経て得られた濾液(充填前溶液)について、容器へ充填する前に、pH測定と、液体クロマトグラフィーによるレベチラセタム量の測定を行い、工程管理を行う。
液体クロマトグラフィーで測定した場合のレベチラセタムの量(定量値)は当該溶液のピーク面積とレベチラセタム標準品500mgを精秤したものを5mlの精製水に溶かしたもののピーク面積との比より算出する。液体クロマトグラフィーの測定条件を以下に示す。
Step (b): Sterilization filtration step The solution obtained in the step (a) is sterilized and filtered. Sterilization filtration can be performed once or more than once, but more than once is preferred. When performing two sterilization filtrations, for example, from the filtrate of the primary sterilization filtration to the container for the next secondary sterilization filtration is aseptically controlled, and after the primary sterilization filtration, the container is filled and sealed. Steps can be performed in a sterile condition. Sterilization filtration is performed by pressure filtration using a Teflon filter having a pore size of 0.2 μm to 0.4 μm, preferably 0.2 μm.
<Measurement of solution before filling>
Before filling the container with the filtrate (solution before filling) obtained through the sterilization filtration, the pH is measured and the amount of levetylacetam is measured by liquid chromatography to control the process.
The amount of levetiracetam (quantitative value) measured by liquid chromatography is calculated from the ratio of the peak area of the solution to the peak area of 500 mg of the standard levetiracetam solution dissolved in 5 ml of purified water. The measurement conditions for liquid chromatography are shown below.
レベチラセタムの定量法:液体クロマトグラフィー
検出器:紫外吸光光度計(測定波長:205nm)
カラム:内径4.6mm、長さ25cmのステンレス管に5μmの液体クロマトグラフィー用シリカゲルを充てんする。
カラム温度:室温
移動相:アセトニトリル/薄めた2mol/L硫酸溶液(1→100)混液(24:1)
流 量:1mL/分
面積測定範囲:レベチラセタムの保持時間の約3倍の範囲
質量への換算は標準品とのピーク面積比より求める。
Quantification method of levetiracetam: Liquid chromatography detector: Ultraviolet absorptiometer (measurement wavelength: 205 nm)
Column: A stainless steel tube having an inner diameter of 4.6 mm and a length of 25 cm is filled with 5 μm of silica gel for liquid chromatography.
Column temperature: Room temperature Mobile phase: Acetonitrile / diluted 2 mol / L sulfuric acid solution (1 → 100) mixed solution (24: 1)
Flow rate: 1 mL / min Area measurement range: Range of about 3 times the holding time of levetiracetam Conversion to mass is calculated from the peak area ratio with the standard product.
<品質調整>
pHが5.53〜5.66、より好ましくは5.55〜5.65であり、かつ液体クロマトグラフィーで測定した場合のレベチラセタムの量の、配合量に対する比(以下「定量値比」)の99.7〜100.4%、より好ましくは99.7〜100.3%である場合は、次の容器充填、密閉、加熱滅菌工程にまわし、最終製品とする。
前記pHおよび定量値比の少なくともいずれかが、前記範囲を外れたロットは、他のロットと合一し、前記工程(b)と同様に滅菌濾過し、前記pHおよび定量値比が前記範囲に含まれることを確認する。すなわち、ロットあわせを行い、滅菌濾過した当該ロットのpHが5.53〜5.66、より好ましくは5.55〜5.65であり、レベチラセタムの液体クロマトグラフィーによる定量値が、配合量の99.7〜100.4%、より好ましくは99.7〜100.3%であることが確認された場合は、最終の充填、密閉、加熱滅菌工程にまわし、最終製品とする。
本明細書において、加熱滅菌は110℃〜125℃で、圧力1〜2気圧で1〜3時間行うことが好ましい。
<Quality adjustment>
The ratio of the amount of levetiracetam to the blended amount (hereinafter referred to as "quantitative value ratio") when the pH is 5.53 to 5.66, more preferably 5.55 to 5.65, and the amount of levetiracetam as measured by liquid chromatography is used. When it is 99.7 to 100.4%, more preferably 99.7 to 100.3%, it is sent to the next container filling, sealing, and heat sterilization steps to obtain the final product.
Lots in which at least one of the pH and the quantitative value ratio is out of the above range are combined with other lots and sterilized and filtered in the same manner as in the step (b), and the pH and the quantitative value ratio are brought into the above range. Make sure it is included. That is, the pH of the lot that was sterilized and filtered after lot matching was 5.53 to 5.66, more preferably 5.55 to 5.65, and the quantitative value of levetiracetam by liquid chromatography was 99 of the blending amount. When it is confirmed that the content is .7 to 100.4%, more preferably 99.7 to 100.3%, the final product is subjected to the final filling, sealing, and heat sterilization steps.
In the present specification, heat sterilization is preferably performed at 110 ° C. to 125 ° C. at a pressure of 1 to 2 atm for 1 to 3 hours.
以下、実施例をあげて、本発明について更に詳細に説明を行う。 Hereinafter, the present invention will be described in more detail with reference to examples.
以下の表2に示すレベチラセタムの注剤用原液の配合処方に従って、秤量装置のついた300Lタンクに処方成分を仕込み、攪拌可溶化し、攪拌下pHをモニターしながら、酢酸を加え、pHが、5.3〜5.7の間に入るように調整した。これに更に精製水を重量が209.3Kgになるまで加え、充分に攪拌し、レベチラセタムの注射剤用原液を得た。なお、レベチラセタムは前記表1に示した規格に適合したものをUCBソシエテ・アノニム社より購入し、用いた。レベチラセタムは、シグマ・アルドリッチ社より購入することも可能である。 According to the formulation of the stock solution for injection of levetiracetam shown in Table 2 below, the formulation components were charged into a 300 L tank equipped with a weighing device, solubilized by stirring, and acetic acid was added while monitoring the pH under stirring to adjust the pH. It was adjusted to be between 5.3 and 5.7. Purified water was further added to this until the weight reached 209.3 kg, and the mixture was sufficiently stirred to obtain a stock solution for injection of levetiracetam. Levetiracetam conforming to the standards shown in Table 1 above was purchased from UCB Society Anonym and used. Levetiracetam can also be purchased from Sigma-Aldrich.
この様に調製したレベチラセタムの注剤用原液は、予め清浄化した状態に保ったラインを通じて、無菌室内の無菌状態に保持した濾過装置に送り込み、0.20μmのポアサイズのテフロンフィルターを用いて滅菌濾過を行い、無菌室内の300Lのタンクに移送した。このタンク内より、再び無菌配管を通じて濾過装置に送り込み、更にもう一回濾過滅菌を行い、300Lタンクに移送した。タンクに移送した溶液を以て注射用溶液とした。レベチラセタムの注射用溶液の一部をサンプリングし、pH値とレベチラセタムの量(定量値)を求めた。液体クロマトグラフィーによるレベチラセタムの定量法は前述のとおりである。残りの注射用溶液は10mlのバイアル瓶に5mlずつ分注し、キャッピングし、密閉した後、120℃、2気圧で1時間最終滅菌を行った。 The stock solution for injection of levetiracetam prepared in this way is sent to a filtration device kept in a sterile state in a sterile room through a line kept in a pre-cleaned state, and sterilized and filtered using a 0.20 μm pore-sized Teflon filter. Was transferred to a 300 L tank in a sterile room. From the inside of this tank, it was sent to the filtration device again through an aseptic pipe, further filtered and sterilized, and transferred to a 300 L tank. The solution transferred to the tank was used as an injection solution. A part of the injectable solution of levetiracetam was sampled, and the pH value and the amount of levetiracetam (quantitative value) were determined. The method for quantifying levetiracetam by liquid chromatography is as described above. The remaining injection solution was dispensed into 10 ml vials in 5 ml increments, capped, sealed, and finally sterilized at 120 ° C. and 2 atm for 1 hour.
上記工程で37ロットの生産を行った。生産品(バイアル瓶)は、生産後48時間に抜き取りを行い、第15改正日本薬局方(PMDA;https://www.pmda.go.jp/files/000163176.pdf)が定める不溶性微粒子試験法の第1法(光遮蔽粒子計測法)に従って、第1法により測定される25μm以上の不溶性微粒子数と、10μm以上の不溶性微粒子数を計測した。結果を表3に示す。
経験上、25μm以上の不溶性微粒子の数が150以下でかつ10μm以上の不溶性微粒子の数が50以下でない場合、注射剤の安全性を損なう可能性が高いことがわかっている。しかるところ、37ロット中、ロットNo.5、No.6及びNo.9がこの基準からはずれ、ロットアウトした。これらのロットを除外する条件はpHが5.53〜5.66であり、レベチラセタムの定量値が、配合量の99.7〜100.4%であることがわかる(表3)。この条件を満たさなくても、上記不溶性微粒子の基準を満足することはあるが、ロットアウトを確実に防ぐためには、上記条件を充足する必要がある。ちなみに、ロットNo.11、No.21、No.34、No.36はいずれも上記条件を満足する。また、上記定量値比の範囲を99.7〜100.3%にするとより確実にロットアウトを防ぐことができる。
37 lots were produced in the above process. The product (vial bottle) is sampled 48 hours after production, and the insoluble fine particle test method specified by the 15th revised Japanese Pharmacopoeia (PMDA; https://www.pmda.go.jp/files/000163176.pdf). The number of insoluble fine particles of 25 μm or more and the number of insoluble fine particles of 10 μm or more measured by the first method were measured according to the first method (light shielding particle measurement method). The results are shown in Table 3.
From experience, it is known that if the number of insoluble fine particles of 25 μm or more is 150 or less and the number of insoluble fine particles of 10 μm or more is not 50 or less, the safety of the injection is likely to be impaired. However, out of 37 lots, lot No. 5, No. 6 and No. 9 deviated from this standard and was lotted out. It can be seen that the conditions for excluding these lots are pH 5.53 to 5.66, and the quantitative value of levetiracetam is 99.7 to 100.4% of the compounding amount (Table 3). Even if this condition is not satisfied, the criteria for insoluble fine particles may be satisfied, but in order to reliably prevent lot-out, it is necessary to satisfy the above conditions. By the way, lot No. 11, No. 21, No. 34, No. All 36 satisfy the above conditions. Further, if the range of the quantitative value ratio is set to 99.7 to 100.3%, lot-out can be prevented more reliably.
本発明はレベチラセタムの注射製剤に適用できる。
The present invention can be applied to an injectable preparation of levetiracetam.
Claims (4)
塩化ナトリウム及び酢酸ナトリウムを含有し、
滅菌濾過が、全成分の溶解後に行う、ポアサイズが0.2μmのフィルターによる滅菌濾過であり、
滅菌濾過後の溶液のpHが5.53〜5.66であり、
前記注射用製剤中のレベチラセタムの量が、配合量の99.7〜100.4%である、注射用滅菌濾過製剤。 Sterilized filtration product for injection containing levetiracetam.
Contains sodium chloride and sodium acetate,
Sterilization filtration is performed after dissolution of all components with a filter having a pore size of 0.2 μm.
The pH of the solution after sterilization filtration is 5.53 to 5.66.
A sterilized filtration preparation for injection, wherein the amount of levetiracetam in the preparation for injection is 99.7 to 100.4% of the blended amount.
(b)工程(a)で得られた溶液をポアサイズが0.2μmのフィルターで滅菌濾過する工程とを含む、注射用滅菌濾過製剤の製造方法であって、
工程(b)の滅菌濾過を経て得られた充填前溶液中のレベチラセタムの量が、工程(a)におけるレベチラセタムの配合量の99.7〜100.4%であり、かつ前記溶液のpHが5.53〜5.66であることを特徴とする、注射用滅菌濾過製剤の製造方法。 (A) Step of blending levetiracetam, sodium chloride and sodium acetate, and
(B) A method for producing a sterile filtered preparation for injection, which comprises a step of sterilizing and filtering the solution obtained in step (a) with a filter having a pore size of 0.2 μm.
The amount of levetiracetam in the pre-filling solution obtained through the sterilization filtration in step (b) is 99.7 to 100.4% of the blended amount of levetiracetam in step (a), and the pH of the solution is 5. A method for producing a sterile filtered preparation for injection, which comprises .53 to 5.66.
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