JP4776115B2 - Manufacturing method of rubber plugs for pharmaceuticals and medical products - Google Patents

Manufacturing method of rubber plugs for pharmaceuticals and medical products Download PDF

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Publication number
JP4776115B2
JP4776115B2 JP2001252562A JP2001252562A JP4776115B2 JP 4776115 B2 JP4776115 B2 JP 4776115B2 JP 2001252562 A JP2001252562 A JP 2001252562A JP 2001252562 A JP2001252562 A JP 2001252562A JP 4776115 B2 JP4776115 B2 JP 4776115B2
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rubber
water
washing
rubber plug
cleaning process
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JP2003062037A (en
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盛皓 須藤
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Daikyo Seiko Ltd
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Daikyo Seiko Ltd
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Description

【0001】
【発明の属する技術分野】
本発明は医薬・医療品用ゴム栓の製造方法に関し、更に詳しくは、ゴム栓への異物や微粒子の付着が著しく低減された高度に清浄な医薬・医療品用ゴム栓の製造方法に関する。
【0002】
【従来の技術】
(背景)
近年、食品への異物混入や、医療ミスなどが社会問題となるなど、食品や医療の安全性への関心が非常に高くなっている。このような社会現象は、当然、今日の医療行為に必要不可欠となっている医薬品へも反映され、現在の医薬品には、高い清浄度のみならず、優れた視認性や操作性までもが求められている。
このような要望は、その包装材料である医薬・医療用ゴム栓にも反映され、現在では、各国の薬局方に適合するばかりでなく、それ以上の品質を有する多種多様な製品を、迅速に製造するシステム(HACCPに対応する)が必要とされている。
【0003】
従来から、清浄度の高い医薬・医療用ゴム栓、即ち、繊維くずや毛髪などの異物(直径あるいは長さが50μm以上で、肉眼で判別可能なものをいう。)や微粒子(直径あるいは長さが50μm未満の肉眼で判別できないものをいう。)の付着が少ない上記ゴム栓を製造するために、製造工程中に洗浄工程を設け、製造工程内で付着した異物および微粒子を洗い流すことにより、自社製品規格や日本薬局方、米国薬局方等の規格を満足する清浄度の高いゴム栓を製造していた。
【0004】
そもそもゴム栓に異物や微粒子が付着するのは、ゴム栓が摩擦により帯電する性質のある高分子物質(ゴム状重合体)から形成されていること及びゴム栓製造工程雰囲気中に異物や微粒子が存在することにある。成形工程で製造されたゴム栓は、最終検査工程を経るまでに、ゴム栓同士、ゴム栓とコンテナー等の他の物品とが接触し、静電気を帯びる。この静電気によって工程雰囲気中の異物や微粒子がゴム栓に付着するのである。帯電を防止する方法として帯電防止剤の使用があるが、ゴム栓には、その使用目的から帯電防止剤を使用することはできない。
従って、洗浄工程で付着物を洗い流すことが最善の方法であるが、洗浄を充分に実施しても特に付着微粒子の除去には限度があり、洗浄だけではより高度な清浄度を有するゴム栓に対する要求に応えられない場合があった。
【0005】
【発明が解決しようとする課題】
本発明はこのような事情に鑑みてなされたものであり、本発明の目的は、従来よりも清浄度が著しく高く(付着異物や微粒子が著しく少ない)、安全性のより高い医薬・医療用ゴム栓を確実、且つ効率よく製造することができる製造方法を提供することである。
本発明者らは、更に高度の清浄度を有するゴム栓の製造方法について鋭意検討した結果、ゴム栓の帯電を防止することは困難であり、一度付着した微粒子を全て除去することも困難なことから、製造過程でゴム栓に付着する異物や微粒子の量を如何に少なくするかということが重要であることを知得し、本発明に至った。
【0006】
【課題を解決するための手段】
本発明によれば、配合・混練工程、成形工程、アルカリ洗浄処理工程、酸洗浄処理工程、温水洗浄処理工程、シャワー洗浄処理工程、乾燥処理工程、及び最終検査工程をこの順に経て、空気清浄度が段階的に高レベルとなる雰囲気下に実施する医薬・医療品用ゴム栓を製造する方法において、前記配合・混練工程を、大気をフィルターを通して、塵埃を除いた大気雰囲気中で実施し、アルカリ洗浄処理工程、酸洗浄処理工程、温水洗浄処理工程の3つの洗浄処理工程を上記の順に1つの処理槽中で、M6.5〜M4.5の空気清浄度雰囲気下で、かつ前記温水洗浄処理工程における洗浄水は、アルカリ洗浄処理工程、及び酸洗浄処理工程における用水よりも清浄度が高い洗浄水で実施し、該処理槽からゴム栓を取り出してシャワー洗浄処理工程に搬送し、該シャワー洗浄処理工程以降の工程をM5.5〜M3.5の空気清浄度雰囲気下にそれぞれ実施する(但し、シャワー洗浄処理工程以降の空気清浄度は洗浄処理工程までの空気清浄度よりも高い)ことを特徴とする清浄な医薬・医療品用ゴム栓を製造する方法が提供される。
【0007】
【発明の実施の形態】
次に発明の好ましい実施の形態を挙げて本発明を更に詳細に説明する。
本発明の医薬・医療品用のゴム栓(以下では単にゴム栓と称することがある。)の製造に使用される材料は、ゴム栓の製造に従来から使用されているゴム材料及びこれを用いたゴム栓と組合わせて使用されているプラスチック材料がいずれも使用でき、特に制限されない。
ゴム材料としては、例えば、ブチルゴム、塩素化ブチルゴム、臭素化ブチルゴム、ジビニルベンゼン共重合ブチルゴムなどのブチル系ゴム、ポリイソプレンゴム(高〜低シス1,4結合)、ポリブタジエンゴム(高〜低シス1,4結合)、スチレン−ブタジエン共重合ゴムなどの共役ジエン系ゴム、エチレン−プロピレン−ジエン三元共重合ゴム(EPDM)、SBSやSISなどの熱可塑性ゴム(TPE)等が挙げられる。プラスチック材料としては、例えば、ポリエチレン、ポリプロピレン、ポリアミド、ポリエステルなどが挙げられる。
【0008】
又、本発明におけるゴム栓は、上記のゴム材料と加硫剤、充填剤および/または補強剤、着色剤、老化防止剤などの配合剤を混練して得られる加硫性ゴム組成物(コンパウンド)を用い、圧縮成形や射出成形などのゴム栓の従来公知の成形方法を用いることによって製造される。使用する配合剤は、従来から医薬品用及び医療具用のゴム栓の製造に使用されているものがいずれも使用でき、特に制限されない。
【0009】
ゴム栓としては、全体が加硫性ゴム組成物のみで製造されたもの、その少なくとも薬品等と接触する面がフッ素樹脂、ポリエチレン等のプラスチックフィルムでラミネートされたもの(プラスチックラミネートゴム栓)、輸液バッグなどのプラスチック製口部に融着により接合させるための上記ゴムとプラスチック部材との組立て成形体などが挙げられるが、本発明においてはゴム栓の形状や構造は特に限定されない。具体的には、例えば、バイアル用ゴム栓(粉末製剤用ゴム栓、液剤用ゴム栓、凍結乾燥製剤用ゴム栓など)、輸液製剤用ゴム栓、注射器用及び容器兼用注射器のピストン(滑栓)やキャップなど、ゴム栓とプラスチック部材との組立成形体(例えば、プルトップ式ゴム栓、上記の輸液バッグ用口部ゴム栓など)などが挙げられる。尚、本発明における医薬・医療品用ゴム栓は、上記のような医薬品用及び医療具用のゴム栓をいう。
【0010】
本発明の医薬・医療品用のゴム栓は、(1)ゴム材料と各種配合剤の秤量及び秤量されたこれらを混練して加硫性ゴム組成物(コンパウンド)を製造する配合・混練工程、(2)得られたコンパウンドをシート状に加工し、このシート状コンパウンドを用いて圧縮成形、射出成形などによって所定の形状及び構造のゴム栓に成形及び加硫し、離型後、得られた多数のゴム栓が連結した成形シートからゴム栓を一個ずつ切り離し、必要により目視による外観検査を行う成形工程、(3)ゴム栓を洗浄して付着物や溶出物を洗い流す洗浄工程、(4)洗浄されたゴム栓を更に洗浄し、乾燥する乾燥工程及び(5)最終検査工程を順に経、適合品とされたゴム栓が袋詰めされ、梱包工程で箱詰めされる。
【0011】
本発明の高度に清浄な医薬・医療品用ゴム栓の製造方法は、成形工程以降の工程を、空気清浄度が段階的に高レベルとなる工程雰囲気で実施することが特徴である。
ゴム栓を製造する作業雰囲気は、理想的には全工程を清浄化された雰囲気下、即ち、クリーンルーム内で実施することであり、空気清浄度のレベルによっては可能である。
【0012】
しかしながら、本発明のゴム栓の製造方法においては、上記のように段階的に空気清浄度が高レベルとなる工程雰囲気中で、成形工程以降の工程を実施するものである。好ましい実施態様は、乾燥工程及び検査工程を成形工程及び洗浄工程よりも清浄度が高いレベルにある工程雰囲気で実施する態様である。更に好ましい実施態様は上記の実施態様に加えて洗浄水の品質も段階的に高品質とする態様である。洗浄水の品質に関しては洗浄工程及び乾燥工程において説明する。
【0013】
ゴム栓製造の最初の工程である配合・混練工程(1)では、原料ゴム及び各種配合剤を秤量し、これらを混合機を用いて混練する。配合時や混練時の配合剤の浮遊を抑制あるいは除去することは困難ではないが、最終製品のゴム栓の清浄度への影響は少ないので、配合混練工程では可視塵埃のない作業雰囲気とすれば充分である。尚、混練工程では、例えば、ニーダー、インターナルミキサーやバンバリーミキサーなどの密閉式混合機の使用が好ましい。混練後、混合機から取り出したコンパウンド(加硫性ゴム組成物)は放冷された後、成形工程に搬送される。
【0014】
成形工程では、ゴム栓の種類によってはコンパウンドを、例えば、フィーダー、ルーダーやロールなどを用いて所定の厚さのシートに加工し、シート状のコンパウンドは熟成及び冷却するために一時的に貯蔵される。
一次貯蔵されたシート状コンパウンドは、圧縮成形や射出成形等の通常のゴム栓の成形に使用される成形機を用い、所定形状の加硫したゴム栓に成形される。ゴム栓は、多数が1枚のシートに連結された状態で離型され、個々に切り離され、必要により目視検査を経て清浄なSUS等の錆びない金属製などのコンテナーに入れられる。
【0015】
成形工程ではシート状コンパウンドおよび離型・分離されたゴム栓が工程雰囲気に曝される。ゴム栓は次の洗浄工程で洗浄されるが、成形工程における付着物を少なくするうえで成形工程の雰囲気は出来るだけ清浄度が高いことが好ましいが、種々検討した結果、以下に説明する空気清浄度レベル1の雰囲気が適当である。コンテナーに入れられたゴム栓は次の洗浄工程に搬送される。
尚、プラスチックラミネートゴム栓以外のゴム栓では、種類によっては、上記の多数のゴム栓が連結した成形シートに架橋(硬化)性シリコーン組成物を塗布し、これを架橋させてゴム栓表面に固着させるシリコーン処理を施す場合がある。しかし、このようなゴム栓も次の洗浄工程を経ることにより未反応のシリコーンは完全に除去され、最終製品の清浄度のレベル低下は防止される。
【0016】
洗浄工程でゴム栓は表面に付着した異物、微粒子などが洗い流される。
本発明の洗浄工程は以下の3つの洗浄処理工程を含んでいる。
(1)ゴム栓を、用水をアルカリ性に調整した洗浄水に浸漬し、高圧水蒸気で処理するアルカリ洗浄処理工程、
(2)アルカリ洗浄されたゴム栓を、用水を酸性に調整した洗浄水で中和処理する酸洗浄処理工程、及び
(3)酸洗浄されたゴム栓を、(2)及び(3)の処理工程における用水よりも高品質の洗浄水で仕上げの洗浄を行う温水洗浄処理工程。
【0017】
本発明においては、上記の3つの処理工程を、従来と同様に、それぞれ独立した3つの処理槽を用いて上記の順に実施することもできるが、処理後に次の処理槽へ順次搬送するときのゴム栓への異物・微粒子の付着を防止し、洗浄効果を高めるために、3つの洗浄処理工程を1つの処理槽中で実施し、次の洗浄処理のためのゴム栓の搬送を行わないことが好ましい。以下では上記の3つの洗浄処理工程を全て1つの処理槽で行う場合について説明する。
【0018】
成形工程から搬送されたゴム栓は、人手によってコンテナーから耐アルカリ性及び耐酸性の洗浄用容器、例えば、ステンレス製の金網かごなどにロット単位で移される。
最初のアルカリ洗浄処理工程(1)は、ゴム栓の表面に付着した汚れ、異物、微粒子、ゴム栓からの溶出物及びパイロジェン(発熱性物質)などを除去する工程である。本処理工程は後述のように加圧下に実施することから、処理槽としてオートクレーブ(好ましくは縦形)が用いられる。洗浄水としては、用水をアルカリ剤、例えば、NaOHでpHを8〜12、好ましくはpH8.5〜11に調整した水溶液(通常、NaOHの0.05〜0.15重量%水溶液)が使用される。アルカリ剤はNaOHに限定されず、これ以外のアルカリ性物質も使用可能である。
【0019】
用水としては、本処理工程(1)及び次の中和処理工程である酸洗浄処理工程(2)においては、井戸水等の原水をイオン交換樹脂や電気的イオン交換(Electroric Deionize Ionization)によるイオン交換水、原水を限外濾過あるいは逆浸透濾過した清浄水も使用できるが、より少ない洗浄回数で、洗浄水による新たな微粒子の付着を回避する上で、好ましくは殺菌した原水を限外濾過または逆浸透濾過した後、前記同様にしてイオン交換した高品質水(それぞれRO水、UF水と称する)の使用である。
【0020】
ゴム栓が入った金網かごをオートクレーブ中のアルカリ性洗浄液に浸漬し、通常、100〜150℃(オートクレーブ内部圧力0〜4kgf/cm2G)、好ましくは110〜145℃、更に好ましくは130〜140℃でゴム栓を処理する。処理時間は、処理温度にもよるが、通常10〜90分である。ゴム栓はそのゴム材料によっては熱劣化するものもあるので、処理温度及び時間は処理効果とゴム栓の劣化を考慮して決めることが必要である。
【0021】
また、アルカリ洗浄処理及び他の洗浄処理も、金網かごなどを縦形オートクレーブの中心軸の回りにゆっくり回転または上下動させて行うが、洗浄処理中にゴム栓同士が自着するブロッキングが生じる場合がある。ブロッキングが生じるとゴム栓同士が自着した部分は洗浄処理が行われず、また、自着の部位によっては洗浄液が乾燥後も残存することにもなることから、ブロッキングはゴム栓の製造効率(歩留)の低下の原因となる。
アルカリ洗浄液の使用形態は、バッチ式、連続式のいずれでもよく、一度使用した洗浄液は、廃液として処理することがゴム栓の清浄度を高めるうえで好ましい。また、洗浄工程で使用する処理槽は、工程雰囲気中の異物や微粒子の落下を防止して金網かごの出し入れを下方部で行えるように、その下部に開閉扉が設けられた縦型処理槽が好ましい。処理槽の構造や形状などは特に限定されない。
【0022】
尚、本発明においては、必要により、アルカリ洗浄処理する前に、イオン交換水などの清浄水も使用できるが、好ましくは前記の高品質水を用いてゴム栓に付着した汚れ、異物や微粒子などを予備的に除去するための前(予備)洗浄処理を行うこともできる。前洗浄処理は上記のオートクレーブ中で実施することもできるが、蓋付き(好ましくは下部に)縦形処理槽内で密閉状態で、室温〜50℃の温度で、前記の金網かごなどを回転又は上下動させながら実施することが、前洗浄処理中に工程雰囲気中の異物や微粒子などが処理槽中へ落下することを防止できるので好ましい。洗浄水はバッチ式又は連続式で、処理槽に加え、前洗浄処理後は廃液として処理することが好ましい。
【0023】
次の酸洗浄処理工程(2)は、アルカリ洗浄処理でゴム栓に付着したアルカリ分を中和する工程であり、アルカリ洗浄液を排出した後、オートクレーブに酸性の中和液を加え、密閉状態で、アルカリ洗浄と同様に金網かごを回転または上下動させて行う。中和液は弱酸性で十分であり、又、中和剤としての酸は特に限定されず、例えば、塩酸等の鉱酸が用いられ、通常、塩酸の0.05重量%水溶液(用水はアルカリ洗浄の場合と同様であり、高品質水の使用が好ましい)が用いられる。処理温度は特に限定されず、通常、室温〜50℃程度で、処理時間は10〜20分程度である。酸洗浄液の使用形態は、バッチ式でも連続式でもよいが、一度使用した酸洗浄液は、廃液として処理することが好ましい。
【0024】
最後の温水洗浄処理工程(3)は、中和処理されたゴム栓を洗浄工程の最後の処理工程として、前記の(1)及び(2)の処理工程における用水よりも清浄度(品質)の高い洗浄水を用い、酸の除去とともに洗浄水中の微粒子が新たにゴム栓に付着することを防止した仕上げの洗浄である。この処理工程も他の処理工程と同様に密閉状態で金網かごを回転または上下動させて行う。温水洗浄の温度は特に制限されないが、通常、室温〜50℃程度の温度である。洗浄水の使用の形態はバッチ式でも連続式でもよい。洗浄水は、前記の高品質も使用出来るが、より少ない洗浄回数で、洗浄水による新たな微粒子の付着を防止するために前記の高品質水を蒸留した最高品質水の使用が好ましい。温水洗浄後、洗浄水はオートクレーブから排出され、廃液として処理することが好ましい。
温水洗浄処理工程終了後、オートクレーブから洗浄液を排出し、ゴム栓はオートクレーブ中で金網かごに入れられたまま十分に水切りされ、次の乾燥工程に搬送される。
【0025】
以上のように洗浄工程においては、洗浄処理中にゴム栓が工程の雰囲気に曝されることはないので、洗浄工程の雰囲気は、空気清浄度レベル1が適当である。
又、洗浄工程における用水は、それに含まれる微粒子が新たにゴム栓に付着することを防止するために、アルカリ洗浄処理及び酸洗浄処理においては前記の高品質水を、温水洗浄処理では上記の最高品質水を使用することが好ましい。さらに、各洗浄処理で使用した洗浄水は、再使用可能であるが、上記のように廃液として処理し、再使用しないことがゴム栓の清浄度を高めるうえで好ましい。
【0026】
洗浄工程に続く乾燥工程は、洗浄工程の最後の温水洗浄処理工程(3)で洗浄されたゴム栓を、さらに前記の温水洗浄処理工程における洗浄水と同等の最高品質の高い洗浄水のシャワーで洗浄するシャワー洗浄処理する工程と洗浄処理されたゴム栓を乾燥させる工程を含んでいる。ここで使用する洗浄水は、温水洗浄処理工程における洗浄水と同様であり、新たな微粒子の付着を防止するうえで前記の最高品質水が好ましい。
【0027】
シャワー洗浄処理工程では、洗浄水による新たな微粒子の付着を防止して前の洗浄工程では除去しきれなかった微粒子の除去をより徹底させるために、例えば、メッシュコンベアーベルトなどで搬送されるゴム栓の全面に最高品質水のシャワーを浴びせ、シャワーの一方向の水流とその衝撃で残留微粒子などを洗い落とす処理工程である。上記の洗浄工程及び乾燥工程におけるシャワー洗浄処理で処理されたゴム栓は、洗浄工程での残留異物や微粒子などがあった場合も、これらは極めて高レベルで除去される。
【0028】
従って、乾燥工程は、洗浄工程までの清浄度レベル1よりも清浄度の高い清浄度レベル2の工程雰囲気下で実施することで、本工程におけるゴム栓への新たな微粒子の付着をより完全に防止することができる。
【0029】
乾燥工程を上記の高レベルの空気清浄度雰囲気で実施することから、シャワー洗浄されたゴム栓の乾燥には、一般的に用いられている熱風による乾燥は、ゴム栓に新たに微粒子などを付着させることになる場合もあるので好ましくなく、遠赤外線の照射および/または高周波を照射して加熱する方法を用いることが好ましい。遠赤外線の照射は、ゴム栓の表面の水の乾燥には適しているが、ゴム栓内部の水の乾燥には適していない。特に好ましい乾燥方法は高周波加熱である。ゴム栓のゴム材料が極性のゴムの場合には高周波によってゴム自体も加熱され、ゴム栓内部の水も表面の水と同時に除去(乾燥)される。ゴム材料が非極性のものでも、使用する配合剤によっては極性の物質も添加されており、そのためにゴム自体も加熱され、極性ゴムの場合と同様の効果が奏される。
高周波加熱の発熱出力は、特に制限されないが、通常1〜5KW程度であり、メッシュコンベアベルトに沿って複数箇所に設置することが乾燥効果を高めるうえで好ましい。乾燥されたゴム栓は検査工程に送られる。
【0030】
本発明において空気清浄度レベル1とは、SIによるクラスがM6.5(米国連邦規格のクラス100,000)〜M4.5(同クラス1,000)をいい、空気清浄度レベル2とは、M5.5(同クラス10,000)〜M3.5(同クラス100)をいう。本発明においては、清浄度レベル2は清浄度レベル1よりも清浄度は高い。可能な限り、いずれの工程も空気清浄度をより高位のレベルとすることが好ましいが、各工程を実施する区域(建屋あるいは部屋)は、それぞれ建坪が大きく、これらの区域の密封性を高めるために費用が嵩み、ゴム栓の製造コストの上昇を招くことから、限度がある。好ましくは、少なくとも成形工程以降の工程を上記の空気清浄度レベルで、更に好ましくは大気圧よりもやや加圧した条件下で実施することである。
【0031】
本発明において洗浄水の品質を段階的に高品質とするということは、前記の洗浄工程における温水洗浄処理工程(3)の洗浄水の品質を、アルカリ洗浄処理工程(1)及び酸洗浄処理工程(2)の用水の品質より高くし、さらに乾燥工程における洗浄処理工程の洗浄水の品質を上記の温水洗浄処理工程(3)の洗浄水と同等以上の清浄度とすることである。
【0032】
前述のように、ゴム栓は摩擦帯電し易い高分子から形成されているので、必要に応じ、成形工程でシート状に加工されたコンパウンド、洗浄工程に付する前のゴム栓、洗浄工程終了後のゴム栓、あるいは乾燥工程を終えたゴム栓などのいずれかを摩擦帯電の大きい工程で除電(帯電除去)処理することが好ましい。更に、工程間のゴム栓の搬送を人手を介さずに無人自動搬送することもゴム栓の清浄度を高めるうえで好ましいことである。
【0033】
除電処理方法としては、非接触でゴム栓の帯電除去処理が可能な工程雰囲気の空気をイオン化させる無声コロナ放電除去器や放射性静電気除去機などの静電除去器を用い、工程雰囲気の空気の電気伝導性を高め、ゴム栓の電荷を空気中に放射して消滅させる方法が好ましい方法として挙げられる。さらに好ましいのはイオン化された空気を直接ゴム栓に吹き付ける送風型である。上記のような静電気除去機は、種々市販されており、適当なものを選択、使用することができ、特に制限されるものではない。又、上記各工程の清浄空気をイオン化して供給することもできる。
【0034】
最後の最終検査工程は、乾燥工程と同じレベル2の空気清浄度雰囲気中で実施される。ゴム栓は、例えば、CCDカメラにより全外観(表面)が自動検査され、成形不良、焼き込み異物などの異物混入、異物付着などの有無を検査し、不適合品は除去、廃棄処分される。この検査ではわからない付着微粒子は、適合品のゴム栓について抜き取り検査で、日本薬局方第13改正の注射剤の不溶性微粒子の試験法に準じて試験され、この試験に適合したロットのゴム栓は、検査工程と同じ雰囲気中でプラスチック製無塵袋に詰め、袋詰めされたゴム栓は梱包工程で箱詰めされる。梱包工程は、特に清浄化された雰囲気でなくともよいが、できれば空気清浄度レベル1の雰囲気中で実施することが好ましい。検査工程では、検査前および/又はあとに除電処理を行い、最後の付着微粒子の除去を行うことが好ましい。
【0035】
本発明のゴム栓の製造においては、人が関与することの多い工程間のゴム栓の搬送は無人自動搬送とすることが好ましい。
無人自動搬送手段としては、例えば、(i)床面下に敷設した誘導路上を電動駆動車を走行させる方式、(ii)天井に設けた軌道に懸垂した状態で、それに設置された電動駆動装置によって移動させる方式などの従来公知の方式による自動搬送手段がいずれも使用でき、自動搬送手段は特に限定されない。全ての工程が同一階で実施される場合は(i) の方式が好ましく、例えば、工程によって1階と2階で実施される場合は上記の2つの方式の併用が好ましい。ゴム栓(コンテナーなどに入れた)の積み降ろしは人手でも、自動化のいずれでもよいが、自動化が好ましい。
尚、無人自動搬送機の運行及び各工程におけるゴム栓の保管管理を、ゴム栓の製造計画に従ってコンピュータ制御することにより、ロット違いや積み忘れなどの人手による搬送で見られるトラブルを確実に防止することができる。
【0036】
【実施例】
以下に実施例及び比較例を挙げて本発明を具体的に説明する。
【0037】
実施例1
塩素化ブチルゴム(エクソンモービル化学社製HT−1066)を用いたバイアル用ゴム栓(天面部(フランジ)の外径(笠径)が19mm、笠厚が3.2mm、足径が13mm、足高が5mm、全高が8.2mm)を圧縮成形により1000個作製した。
前記の配合・混練工程は大気をフィルターを通して塵埃を除いた大気雰囲気中で、前記の成形工程及び洗浄工程はM6.5の清浄雰囲気中で、前記の乾燥工程及び検査工程はM5.5の清浄空気雰囲気中で実施した。
【0038】
洗浄工程は下蓋付きオートクレーブを用いて行った。最初のアルカリ洗浄処理は、用水として殺菌した井戸水を逆浸透膜で濾過し、次いで電気交換式純水製造装置でイオン交換した高品質水を用い、これに苛性ソーダを0.1%濃度に溶解したアルカリ水を使用した。オートクレーブに上記のゴム栓を入れた円筒状のステンレス製金網かごを挿入し、下蓋を閉め、アルカリ水をゴム栓の全容積の3倍量充填し、金網かごを5回/分のレートで上下動させながら内温を160℃に上げ、沸騰下に1時間処理した。加熱を止め、液温を80℃まで冷却してからアルカリ洗浄水を排出した。
【0039】
次に、上記の高品質水の0.05%塩酸水溶液(室温)を上記同様オートクレーブに充填し、金網かごを上下動させながら、加温せずに酸洗浄を10分間行った。その後、酸洗浄液を排出し、金網かごを引き続き上下動させて水切りを行った。
最後に、上記の高品質水の蒸留水である最高品質水を上記同様オートクレーブに充填し、加温せずに10分間金網かごを上下動させて洗浄した。洗浄水を排出し、水切りした後オートクレーブの下蓋を開け金網かごを取り出した。
【0040】
洗浄工程を終えたゴム栓を金網かご毎、次の乾燥工程へ無人自動搬送機で搬送した。M5.5の清浄化された雰囲気の乾燥工程で、金網からゴム栓を人手でホッパーへ移し、次の検査工程にまで至るステンレス製メッシュコンベヤーにゴム栓同士が重ならないように自動化されたフィーダーでゴム栓を載置した。
ここでは、先ずゴム栓はコンベヤーの進行につれて、シャワー洗浄ゾーンで最初にコンベヤーの上方から、次いで下方から、それぞれ一方向の最高品質水によるシャワーで合計15秒間洗浄され、自然落下で水切りされながらゴム栓は乾燥ゾーンに至り、ここで高周波加熱装置からの高周波で加熱、乾燥され、ゴム栓は検査工程に運ばれる。シャワー洗浄水は、上記の最高品質水を用いた。
【0041】
M5.5の清浄度雰囲気の検査工程に乾燥工程からメッシュコンベヤーでゴム栓は搬送される。
上記の洗浄工程においては、洗浄前の、洗浄工程終了後の、また検査工程では全工程を終えたゴム栓を、それぞれ適宜10個抜き取り、無塵袋に収納し、クラス1,000の試験室でそれぞれのゴム栓の微粒子付着個数を下記の方法で測定した。尚、洗浄工程終了後のゴム栓は検査室で高周波加熱により乾燥させた。
【0042】
〔微粒子数の測定方法〕
日本薬局方第13改正(第一追補)の一般試験法64.注射剤の不溶性微粒子試験法に準じ、光遮蔽型自動微粒子測定装置(RION KL−01:リオン社製自動微粒子計測器)を用いて不溶性微粒子の個数を測定した。
抜き取った10個のゴム栓をピンセットで500ml用特注硬質ガラス製バイアルに入れ、0.4μm次いで0.2μmのフィルターを通した無塵水300mlを加え、シーロンフィルム(富士フィルム社製)でシールし、ゴム栓がおおよそ1秒間に2回転するように手で20秒間振とうさせた。1時間静置後、内溶液を10ml採取し、測定する。同様にして合計3回測定し、その平均値を求めた。結果を表1に示す。
【0043】
比較例1
成形工程及び洗浄工程の空気清浄度を配合・混練工程の空気清浄度とし、乾燥工程をM6.5の清浄度雰囲気で実施する以外は実施例1と同様にしてゴム栓1000個を作製した。実施例1と同様にして微粒子の個数を測定した。結果を表1に示した。
【0044】
比較例2
成形工程から乾燥工程までをM6.5の清浄度雰囲気下に、検査工程をM5.5の清浄度雰囲気下に実施する以外は実施例1と同様にして1000個のゴム栓を作製し、微粒子の個数を測定した。結果を表1に示した。
【0045】
比較例3
成形工程及び洗浄工程を配合・混練工程の空気清浄度雰囲気下に、乾燥工程以降をM5.5の清浄度雰囲気下に実施する以外は実施例1と同様にして1000個のゴム栓を作製し、微粒子の個数を測定した。結果を表1に示した。
【0046】
実施例2
最終検査工程で実施例1のゴム栓100個を抜き取り、イオンブローにより除電処理し、10個を抜き取り、実施例1と同様にして微粒子個数を測定した。その結果を表1に示した。

Figure 0004776115
【0047】
【発明の効果】
以上の如き本発明により、各工程の雰囲気の空気の清浄度を前記レベルに管理し、洗浄工程などで使用する洗浄水の清浄度を検査工程に近づくほど高め、さらに除電処理を組み合わせることで、従来に比べて格段に清浄度の高い(異物および微粒子付着量が著減した)医薬・医療用ゴム栓を製造することができる。[0001]
BACKGROUND OF THE INVENTION
The present invention relates to a method for producing a rubber plug for pharmaceuticals / medical products, and more particularly to a method for producing a highly clean rubber plug for pharmaceuticals / medical products in which adhesion of foreign matter and fine particles to the rubber plug is significantly reduced.
[0002]
[Prior art]
(background)
In recent years, there has been a great interest in food and medical safety, such as the inclusion of foreign substances in food and medical mistakes becoming social issues. Naturally, these social phenomena are also reflected in pharmaceuticals that are indispensable for today's medical practice, and today's pharmaceuticals require not only high cleanliness but also excellent visibility and operability. It has been.
Such requests are also reflected in the medical and medical rubber stoppers that are the packaging materials, and now, not only conforms to the pharmacopoeia of each country, but also a wide variety of products with higher quality can be quickly There is a need for a manufacturing system (corresponding to HACCP).
[0003]
Conventionally, medical and medical rubber plugs with high cleanliness, that is, foreign matters such as fiber scraps and hair (diameter or length of 50 μm or more, which can be identified with the naked eye) and fine particles (diameter or length). In order to manufacture the rubber plug, there is a cleaning process in the manufacturing process, and the foreign substances and fine particles adhering in the manufacturing process are washed away. We manufactured rubber plugs with high cleanliness that satisfy product standards, Japanese Pharmacopoeia, US Pharmacopoeia standards, etc.
[0004]
In the first place, foreign matters and fine particles adhere to the rubber plug because the rubber plug is formed of a polymer material (rubber-like polymer) that has a property of being charged by friction, and the foreign matter and fine particles are in the rubber plug manufacturing process atmosphere. It exists to exist. The rubber plugs manufactured in the molding process are charged with static electricity due to contact between the rubber plugs and the rubber plugs and other articles such as containers before the final inspection process. This static electricity causes foreign matter and fine particles in the process atmosphere to adhere to the rubber plug. An antistatic agent is used as a method for preventing electrification, but an antistatic agent cannot be used for a rubber plug for the purpose of use.
Therefore, it is the best method to wash away the deposits in the washing process, but even if the washing is carried out sufficiently, there is a limit to the removal of the adhering fine particles. In some cases, the request could not be met.
[0005]
[Problems to be solved by the invention]
The present invention has been made in view of such circumstances, and an object of the present invention is to provide a medical / medical rubber that is significantly higher in cleanliness (contaminated foreign matter and fine particles are significantly less) and safer than before. It is an object of the present invention to provide a production method capable of producing a stopper reliably and efficiently.
As a result of intensive studies on a method for producing a rubber plug having a higher degree of cleanliness, the present inventors have found that it is difficult to prevent the rubber plug from being charged, and it is also difficult to remove all the fine particles once adhered. From this, it was learned that it is important how to reduce the amount of foreign matter and fine particles adhering to the rubber plug during the manufacturing process, and the present invention has been achieved.
[0006]
[Means for Solving the Problems]
According to the present invention, the air cleanliness through the blending / kneading process, the molding process, the alkali cleaning process, the acid cleaning process, the hot water cleaning process, the shower cleaning process, the drying process, and the final inspection process in this order. In a method for producing a rubber stopper for a pharmaceutical / medical product that is carried out in an atmosphere in which the level gradually increases, The blending and kneading step is carried out in an air atmosphere excluding dust through the air through a filter, Three washing treatment steps of alkaline washing treatment step, acid washing treatment step, and warm water washing treatment step are performed in one treatment tank in the above order. In the air cleanliness atmosphere of M6.5 to M4.5, the washing water in the warm water washing treatment step is washing water having a higher degree of cleanliness than the water used in the alkali washing treatment step and the acid washing treatment step. The rubber stopper is taken out from the treatment tank and transported to the shower cleaning process, and the steps after the shower cleaning process are performed. M5.5 to M3.5 In an air cleanliness atmosphere Respectively carry out (However, the air cleanliness after the shower cleaning process is higher than the air cleanliness until the cleaning process) There is provided a method for producing a clean medical / medical rubber stopper.
[0007]
DETAILED DESCRIPTION OF THE INVENTION
Next, the present invention will be described in more detail with reference to preferred embodiments of the invention.
The material used for the manufacture of the rubber plug for the pharmaceutical / medical product of the present invention (hereinafter sometimes simply referred to as a rubber plug) is a rubber material conventionally used for the manufacture of the rubber plug and the material used therefor. Any plastic material used in combination with a conventional rubber stopper can be used and is not particularly limited.
Examples of rubber materials include butyl rubber such as butyl rubber, chlorinated butyl rubber, brominated butyl rubber, divinylbenzene copolymer butyl rubber, polyisoprene rubber (high to low cis 1,4 bond), and polybutadiene rubber (high to low cis 1). , 4-bond), conjugated diene rubbers such as styrene-butadiene copolymer rubber, ethylene-propylene-diene terpolymer rubber (EPDM), thermoplastic rubber (TPE) such as SBS and SIS, and the like. Examples of the plastic material include polyethylene, polypropylene, polyamide, and polyester.
[0008]
The rubber plug in the present invention is a vulcanizable rubber composition (compound) obtained by kneading the above rubber material and a compounding agent such as a vulcanizing agent, a filler and / or a reinforcing agent, a coloring agent, and an anti-aging agent. ) And using a conventionally known molding method for rubber plugs such as compression molding and injection molding. As the compounding agent to be used, any of those conventionally used for producing rubber stoppers for pharmaceuticals and medical devices can be used, and is not particularly limited.
[0009]
Rubber plugs made entirely of a vulcanizable rubber composition, at least a surface that comes into contact with chemicals, etc. laminated with a plastic film such as fluororesin or polyethylene (plastic laminated rubber plug), infusion solution Examples include an assembly molded body of the rubber and the plastic member for joining to a plastic mouth such as a bag by fusion, but the shape and structure of the rubber plug are not particularly limited in the present invention. Specifically, for example, rubber stoppers for vials (rubber stoppers for powder preparations, rubber stoppers for liquid preparations, rubber stoppers for freeze-dried preparations, etc.), rubber stoppers for infusion preparations, pistons for syringes and container-use syringes (slip stoppers) And an assembly molded body of a rubber plug and a plastic member (for example, a pull-top type rubber plug, the above-described infusion bag mouth rubber plug, etc.) and the like. In addition, the rubber plug for medicines and medical products in the present invention refers to the rubber plug for pharmaceuticals and medical devices as described above.
[0010]
The rubber plug for a pharmaceutical / medical product of the present invention comprises: (1) a blending and kneading step for producing a vulcanizable rubber composition (compound) by kneading the weighed and weighed rubber materials and various compounding agents; (2) The obtained compound was processed into a sheet shape, molded and vulcanized into a rubber plug of a predetermined shape and structure by compression molding, injection molding, etc. using this sheet compound, and obtained after release A molding process in which the rubber plugs are separated one by one from a molded sheet connected with a large number of rubber plugs, and the visual inspection is visually inspected as necessary. (3) A cleaning process in which the rubber plugs are washed to wash off deposits and eluate. (4) The washed rubber stopper is further washed and dried, and (5) the final inspection process is sequentially performed, and the rubber stopper made into a conforming product is packaged and boxed in the packaging process.
[0011]
The manufacturing method of the highly clean rubber plug for medical / medical products according to the present invention is characterized in that the steps after the molding step are performed in a process atmosphere in which the air cleanliness is gradually increased.
The working atmosphere for manufacturing the rubber plug is ideally carried out in a clean atmosphere, that is, in a clean room, depending on the level of air cleanliness.
[0012]
However, in the rubber plug manufacturing method of the present invention, the steps after the molding step are carried out in the process atmosphere in which the air cleanliness gradually increases as described above. A preferable embodiment is an embodiment in which the drying process and the inspection process are performed in a process atmosphere having a higher level of cleanliness than the molding process and the cleaning process. A more preferred embodiment is a mode in which the quality of the washing water is gradually improved in addition to the above embodiment. The quality of the cleaning water will be described in the cleaning process and the drying process.
[0013]
In the blending / kneading step (1), which is the first step of rubber plug production, raw rubber and various compounding agents are weighed and kneaded using a mixer. Although it is not difficult to suppress or remove the floating of the compounding agent at the time of compounding or kneading, it has little effect on the cleanliness of the rubber plug of the final product, so if the working atmosphere is free of visible dust in the compounding kneading process It is enough. In the kneading step, it is preferable to use a closed mixer such as a kneader, an internal mixer or a Banbury mixer. After kneading, the compound (vulcanizable rubber composition) taken out from the mixer is allowed to cool and then conveyed to the molding step.
[0014]
In the molding process, depending on the type of rubber plug, the compound is processed into a sheet having a predetermined thickness using, for example, a feeder, a ruder or a roll, and the sheet-like compound is temporarily stored for aging and cooling. The
The primarily stored sheet-like compound is molded into a vulcanized rubber plug having a predetermined shape using a molding machine used for molding a normal rubber plug such as compression molding or injection molding. The rubber plugs are released in a state where many of them are connected to a single sheet, are individually cut off, and are put into a container made of rust-free metal such as SUS after visual inspection if necessary.
[0015]
In the molding process, the sheet-like compound and the rubber plug separated and separated are exposed to the process atmosphere. The rubber plug is cleaned in the next cleaning process, but it is preferable that the atmosphere of the molding process is as clean as possible in order to reduce deposits in the molding process, but as a result of various studies, the air cleaning described below A level 1 atmosphere is appropriate. The rubber stopper placed in the container is transported to the next cleaning process.
For rubber plugs other than plastic laminated rubber plugs, depending on the type, a cross-linked (curing) silicone composition is applied to a molded sheet connected with the above-mentioned many rubber plugs, and this is cross-linked to adhere to the rubber plug surface. In some cases, silicone treatment is performed. However, such a rubber plug is also subjected to the following washing process, whereby unreacted silicone is completely removed, and a reduction in the level of cleanliness of the final product is prevented.
[0016]
In the cleaning process, the rubber plug is washed away of foreign matters and fine particles adhering to the surface.
The cleaning process of the present invention includes the following three cleaning processes.
(1) An alkaline cleaning treatment step in which the rubber plug is immersed in cleaning water whose alkaline water is adjusted to alkaline and treated with high-pressure steam;
(2) an acid washing treatment step of neutralizing the alkali-washed rubber stopper with washing water adjusted to be acidic, and
(3) A warm water washing treatment step of washing the acid-washed rubber stopper with a higher quality washing water than the water used in the treatment steps (2) and (3).
[0017]
In the present invention, the above three processing steps can be carried out in the above order using three independent processing tanks, respectively, as in the prior art, but when sequentially transported to the next processing tank after processing. In order to prevent foreign matter and fine particles from adhering to the rubber plug and enhance the cleaning effect, three cleaning processes must be performed in one processing tank, and the rubber plug should not be transported for the next cleaning process. Is preferred. Below, the case where all the above-mentioned three washing processing steps are performed in one processing tank is explained.
[0018]
The rubber stopper transported from the molding process is manually transferred from the container to an alkali- and acid-resistant cleaning container such as a stainless steel wire mesh basket.
The first alkali cleaning treatment step (1) is a step of removing dirt, foreign matter, fine particles, eluate from the rubber plug, pyrogen (pyrogenic substance) and the like attached to the surface of the rubber plug. Since this treatment step is performed under pressure as described later, an autoclave (preferably a vertical shape) is used as a treatment tank. As the washing water, an aqueous solution (usually 0.05 to 0.15% by weight aqueous solution of NaOH) in which the water is adjusted to an alkaline agent, for example, NaOH with a pH of 8 to 12, preferably pH 8.5 to 11, is used. The The alkaline agent is not limited to NaOH, and other alkaline substances can be used.
[0019]
As water for use, in this treatment step (1) and the next neutralization treatment step (2), raw water such as well water is ion-exchanged by ion exchange resin or electric ion exchange (Electronic Deionize Ionization). Purified water obtained by ultrafiltration or reverse osmosis filtration of water and raw water can also be used. However, in order to avoid the adhering of new fine particles due to the washing water with a smaller number of washings, preferably, the sterilized raw water is subjected to ultrafiltration or reverse filtration. This is the use of high-quality water (referred to as RO water and UF water, respectively) ion-exchanged in the same manner as described above after osmotic filtration.
[0020]
A wire mesh basket containing a rubber stopper is immersed in an alkaline cleaning solution in an autoclave and is usually 100 to 150 ° C. (autoclave internal pressure is 0 to 4 kgf / cm). 2 G), preferably the rubber plug is treated at 110 to 145 ° C, more preferably 130 to 140 ° C. The treatment time is usually 10 to 90 minutes although it depends on the treatment temperature. Some rubber plugs are subject to thermal degradation depending on the rubber material, so the treatment temperature and time must be determined in consideration of the treatment effect and the degradation of the rubber plug.
[0021]
Alkaline cleaning and other cleaning processes are also performed by slowly rotating or vertically moving a wire mesh basket or the like around the central axis of a vertical autoclave. However, blocking may occur where rubber plugs adhere to each other during the cleaning process. is there. When blocking occurs, the parts where the rubber plugs are self-attached are not cleaned, and depending on the part of the self-adhesion, the cleaning liquid may remain after drying. Cause a decrease in
The use form of the alkaline cleaning liquid may be either a batch type or a continuous type, and the cleaning liquid once used is preferably treated as a waste liquid in order to increase the cleanliness of the rubber stopper. In addition, the processing tank used in the cleaning process is a vertical processing tank with an open / close door at the bottom so that foreign matter and fine particles in the process atmosphere can be prevented and the wire mesh basket can be taken in and out at the lower part. preferable. The structure and shape of the treatment tank are not particularly limited.
[0022]
In the present invention, if necessary, clean water such as ion-exchanged water can also be used before the alkali cleaning treatment. Preferably, dirt, foreign matter, fine particles, etc. attached to the rubber stopper using the high-quality water are used. A preliminary (preliminary) cleaning process for preliminarily removing can also be performed. The pre-cleaning treatment can be carried out in the above autoclave, but the above-mentioned wire mesh cage is rotated or moved up and down at a temperature of room temperature to 50 ° C. in a sealed state (preferably at the bottom) in a vertical processing tank. It is preferable to carry out the movement because foreign substances and fine particles in the process atmosphere can be prevented from falling into the treatment tank during the pre-cleaning treatment. The washing water is batch type or continuous type, and is preferably treated as a waste liquid after the pre-cleaning treatment in addition to the treatment tank.
[0023]
The next acid cleaning treatment step (2) is a step of neutralizing the alkali adhering to the rubber plug by the alkali cleaning treatment. After discharging the alkali cleaning solution, an acidic neutralizing solution is added to the autoclave, In the same manner as alkali cleaning, the wire mesh basket is rotated or moved up and down. The neutralizing solution is weakly acidic and sufficient, and the acid as the neutralizing agent is not particularly limited. For example, a mineral acid such as hydrochloric acid is used, and usually a 0.05 wt% aqueous solution of hydrochloric acid (the water used is alkaline). As in the case of washing, use of high-quality water is preferable. The treatment temperature is not particularly limited, and is usually about room temperature to 50 ° C., and the treatment time is about 10 to 20 minutes. The use form of the acid cleaning liquid may be either a batch type or a continuous type, but the acid cleaning liquid once used is preferably treated as a waste liquid.
[0024]
In the final hot water washing treatment step (3), the neutralized rubber plug is used as the last treatment step of the washing step, and the cleanliness (quality) is higher than that of the water used in the treatment steps (1) and (2). This is a finishing wash that uses high washing water and removes acid and prevents particles in the washing water from newly adhering to the rubber stopper. This processing step is performed by rotating or moving up and down the wire mesh cage in a sealed state like the other processing steps. The temperature of the hot water washing is not particularly limited, but is usually about room temperature to about 50 ° C. The washing water may be used either batchwise or continuously. Although the above-mentioned high quality can be used as the washing water, it is preferable to use the highest quality water obtained by distilling the above high-quality water in order to prevent adhesion of new fine particles by the washing water with a smaller number of washings. After washing with warm water, the washing water is preferably discharged from the autoclave and treated as a waste liquid.
After completion of the hot water washing treatment process, the washing solution is discharged from the autoclave, and the rubber stopper is sufficiently drained while being put in the wire mesh basket in the autoclave, and conveyed to the next drying process.
[0025]
As described above, in the cleaning process, since the rubber plug is not exposed to the process atmosphere during the cleaning process, an air cleanliness level of 1 is appropriate for the atmosphere of the cleaning process.
In addition, the water used in the washing process prevents the fine particles contained therein from newly adhering to the rubber plug, so that the high-quality water is used in the alkali washing treatment and the acid washing treatment, and the above-mentioned highest in the hot water washing treatment. It is preferred to use quality water. Furthermore, although the washing water used in each washing treatment can be reused, it is preferable to treat it as a waste liquid as described above and not reuse it in order to increase the cleanliness of the rubber plug.
[0026]
In the drying process following the cleaning process, the rubber stopper cleaned in the last hot water cleaning process (3) of the cleaning process is further showered with the highest quality cleaning water equivalent to the cleaning water in the hot water cleaning process. It includes a step of performing a shower cleaning process for cleaning and a step of drying the cleaned rubber stopper. The washing water used here is the same as the washing water in the warm water washing treatment step, and the above-mentioned highest quality water is preferable in preventing the adhesion of new fine particles.
[0027]
In the shower cleaning process, for example, rubber plugs that are transported by a mesh conveyor belt, etc., in order to prevent new particles from adhering to the cleaning water and more thoroughly remove particles that could not be removed in the previous cleaning process This is a treatment process in which a shower of the highest quality water is taken over the entire surface, and residual particulates are washed away by the unidirectional water flow and the impact of the shower. The rubber stopper processed by the shower cleaning process in the cleaning process and the drying process is removed at a very high level even when there are residual foreign matters or fine particles in the cleaning process.
[0028]
Therefore, the drying process is performed in a process atmosphere of a cleanliness level 2 that is higher than the cleanliness level 1 up to the cleaning process, so that the adhesion of new fine particles to the rubber plug in this process is more complete. Can be prevented.
[0029]
Since the drying process is performed in the above-mentioned high-level air cleanliness atmosphere, the shower-washed rubber plug is dried with hot air, which is commonly used. In some cases, it is not preferable, and it is preferable to use a method of heating by irradiation with far infrared rays and / or irradiation with high frequency. Far-infrared irradiation is suitable for drying water on the surface of the rubber plug, but is not suitable for drying water inside the rubber plug. A particularly preferable drying method is high-frequency heating. When the rubber material of the rubber plug is a polar rubber, the rubber itself is also heated by the high frequency, and the water inside the rubber plug is removed (dried) simultaneously with the water on the surface. Even if the rubber material is non-polar, a polar substance is also added depending on the compounding agent to be used. For this reason, the rubber itself is heated, and the same effect as in the case of the polar rubber is exhibited.
The heat output of the high-frequency heating is not particularly limited, but is usually about 1 to 5 kW, and it is preferable to install at a plurality of locations along the mesh conveyor belt in order to enhance the drying effect. The dried rubber stopper is sent to the inspection process.
[0030]
In the present invention, the air cleanliness level 1 means that the SI class is M6.5 (US federal standard class 100,000) to M4.5 (same class 1,000), and the air cleanliness level 2 is M5.5 (same class 10,000) to M3.5 (same class 100). In the present invention, the cleanliness level 2 is higher than the cleanliness level 1. As much as possible, it is preferable for each process to have a higher level of air cleanliness. However, the areas (buildings or rooms) where each process is carried out have a large floor area, in order to improve the sealing performance of these areas. However, there is a limit because the cost increases and the manufacturing cost of the rubber plug increases. Preferably, at least the steps after the molding step are performed at the above air cleanliness level, and more preferably under a condition slightly pressurized from atmospheric pressure.
[0031]
In the present invention, the quality of the washing water is gradually improved, which means that the quality of the washing water in the warm water washing treatment step (3) in the washing step is the same as that in the alkali washing treatment step (1) and the acid washing treatment step. The quality of the water used in (2) should be higher, and the quality of the washing water in the washing process in the drying process should be equal to or higher than the washing water in the warm water washing process (3).
[0032]
As mentioned above, the rubber plug is made of a polymer that is easily triboelectrically charged, so if necessary, the compound processed into a sheet in the molding process, the rubber plug before being subjected to the cleaning process, and after the cleaning process is completed It is preferable that any one of the rubber plug or the rubber plug after the drying process is subjected to charge removal (charge removal) treatment in a process having a large frictional charge. Furthermore, it is also preferable to increase the cleanliness of the rubber plug by unattended automatic transfer of the rubber plug between processes without human intervention.
[0033]
As a charge removal treatment method, an electrostatic remover such as a silent corona discharge remover or a radioactive static eliminator that ionizes process atmosphere air that can be charged and removed without contact with a rubber plug is used. A preferred method is to increase the conductivity and radiate the charge of the rubber plug into the air to eliminate it. Further preferred is a blower type in which ionized air is blown directly onto a rubber stopper. Various types of static eliminators as described above are commercially available, and appropriate ones can be selected and used, and are not particularly limited. Moreover, the clean air of each said process can also be ionized and supplied.
[0034]
The final final inspection step is performed in the same level 2 air cleanliness atmosphere as the drying step. For example, the entire appearance (surface) of the rubber plug is automatically inspected by a CCD camera, inspected for the presence of molding defects, foreign matters such as burn-in foreign matter, foreign matter adhesion, etc., and nonconforming products are removed and discarded. Adherent particulates that are not known in this inspection are tested in accordance with the test method for insoluble fine particles of injectables in the 13th revision of the Japanese Pharmacopoeia. The rubber stopper packed in a plastic dust-free bag in the same atmosphere as the inspection process is boxed in the packing process. The packing process does not have to be a particularly cleaned atmosphere, but is preferably performed in an atmosphere of air cleanliness level 1 if possible. In the inspection step, it is preferable to perform a charge removal process before and / or after the inspection to remove the last adhered fine particles.
[0035]
In the production of the rubber plug of the present invention, it is preferable that unmanned automatic conveyance be used for the conveyance of the rubber plug between processes in which people are often involved.
As the unmanned automatic transfer means, for example, (i) a method of running an electrically driven vehicle on a taxiway laid under the floor, (ii) an electric drive device installed in the suspension suspended on a track provided on the ceiling Any of the conventionally known automatic conveying means such as a method of moving by the above can be used, and the automatic conveying means is not particularly limited. When all steps are performed on the same floor, the method (i) is preferable. For example, when the steps are performed on the first floor and the second floor, the combination of the above two methods is preferable. The loading and unloading of the rubber stopper (in a container or the like) may be performed manually or automatically, but automation is preferable.
In addition, the operation of unmanned automatic transfer machines and the storage management of rubber plugs in each process are controlled by a computer according to the rubber plug manufacturing plan, thereby reliably preventing troubles seen in manual transport such as lot differences and forgotten loading. be able to.
[0036]
【Example】
The present invention will be specifically described below with reference to examples and comparative examples.
[0037]
Example 1
Rubber stopper for vials using chlorinated butyl rubber (HT-1066 manufactured by ExxonMobil Chemical Co., Ltd.) (top diameter (flange) outer diameter (shade diameter) is 19 mm, shade thickness is 3.2 mm, foot diameter is 13 mm, foot height) Was 5 mm, and the total height was 8.2 mm).
The blending and kneading process is performed in an air atmosphere in which air is removed through a filter to remove dust, the molding process and the cleaning process are performed in a clean atmosphere of M6.5, and the drying process and the inspection process are cleaned of M5.5. Conducted in an air atmosphere.
[0038]
The washing step was performed using an autoclave with a lower lid. In the first alkali cleaning treatment, the well water sterilized as working water is filtered through a reverse osmosis membrane, and then ion-exchanged high-quality water is used in an electric exchange type pure water production apparatus, and caustic soda is dissolved in a concentration of 0.1%. Alkaline water was used. Insert the cylindrical stainless steel wire cage with the above rubber stopper into the autoclave, close the bottom lid, and fill with alkaline water 3 times the total volume of the rubber stopper, and fill the wire mesh cage at a rate of 5 times / minute. The internal temperature was raised to 160 ° C. while moving up and down, and the mixture was treated for 1 hour under boiling. Heating was stopped, the liquid temperature was cooled to 80 ° C., and then the alkaline washing water was discharged.
[0039]
Next, 0.05% hydrochloric acid aqueous solution (room temperature) of the above-mentioned high quality water was filled in the autoclave in the same manner as above, and acid washing was performed for 10 minutes without heating while moving the wire cage up and down. Thereafter, the acid cleaning liquid was discharged, and the wire mesh basket was continuously moved up and down to drain water.
Finally, the highest-quality water, which is the distilled water of the above-mentioned high-quality water, was filled in the autoclave in the same manner as described above, and washed by moving the wire mesh basket up and down for 10 minutes without heating. After washing water was drained and drained, the lower lid of the autoclave was opened and the wire mesh basket was taken out.
[0040]
The rubber stopper after the cleaning process was transported to the next drying process for each wire mesh cage by an unattended automatic transport machine. With a feeder that is automated so that the rubber plugs do not overlap each other on the stainless steel mesh conveyor that is manually transferred from the wire mesh to the hopper in the M5.5's clean atmosphere drying process. A rubber stopper was placed.
Here, the rubber plug is first washed in the shower cleaning zone from the top of the conveyor and then from the bottom in the shower cleaning zone for 15 seconds in total with a shower of the highest quality water in one direction, and the rubber plug is drained by natural fall. The plug reaches the drying zone, where it is heated and dried with high frequency from a high frequency heating device, and the rubber plug is carried to the inspection process. The highest quality water described above was used as the shower washing water.
[0041]
The rubber stopper is conveyed by the mesh conveyor from the drying process to the inspection process of the cleanliness atmosphere of M5.5.
In the above cleaning process, 10 rubber plugs are removed as needed before cleaning, after completion of the cleaning process, and after the completion of all processes in the inspection process, and stored in a dust-free bag. Then, the number of fine particles attached to each rubber plug was measured by the following method. The rubber stopper after the cleaning process was dried by high-frequency heating in the inspection room.
[0042]
[Method for measuring the number of fine particles]
General test method of Japanese Pharmacopoeia 13th revision (first supplement) 64. According to the insoluble fine particle test method for injections, the number of insoluble fine particles was measured using a light shielding type automatic fine particle measuring apparatus (RION KL-01: automatic fine particle measuring instrument manufactured by Rion Co., Ltd.).
Ten rubber stoppers taken out are put into a 500 ml custom hard glass vial with tweezers, 0.4 μm and then 300 ml of dust-free water passed through a 0.2 μm filter are added and sealed with a Ceylon film (Fuji Film). The rubber plug was shaken by hand for 20 seconds so that the rubber plug rotated approximately twice per second. After standing for 1 hour, 10 ml of the internal solution is taken and measured. Similarly, the measurement was performed three times in total, and the average value was obtained. The results are shown in Table 1.
[0043]
Comparative Example 1
1000 rubber plugs were produced in the same manner as in Example 1 except that the air cleanliness of the molding process and the cleaning process was the air cleanliness of the blending / kneading process, and the drying process was performed in a clean atmosphere of M6.5. The number of fine particles was measured in the same manner as in Example 1. The results are shown in Table 1.
[0044]
Comparative Example 2
1000 rubber plugs were prepared in the same manner as in Example 1 except that the molding process to the drying process were performed in an M6.5 clean atmosphere, and the inspection process was performed in an M5.5 clean atmosphere. The number of was measured. The results are shown in Table 1.
[0045]
Comparative Example 3
1000 rubber plugs were prepared in the same manner as in Example 1 except that the molding process and the cleaning process were performed in an air cleanliness atmosphere of the blending and kneading process, and the drying process and subsequent processes were performed in an M5.5 cleanliness atmosphere. The number of fine particles was measured. The results are shown in Table 1.
[0046]
Example 2
In the final inspection step, 100 rubber plugs of Example 1 were extracted, subjected to charge removal by ion blowing, 10 were extracted, and the number of fine particles was measured in the same manner as in Example 1. The results are shown in Table 1.
Figure 0004776115
[0047]
【The invention's effect】
By the present invention as described above, the cleanliness of the air in the atmosphere of each process is controlled to the above level, and the cleanliness of the cleaning water used in the cleaning process and the like is increased as it approaches the inspection process, and further by combining the static elimination treatment, It is possible to manufacture a medical / medical rubber stopper that is remarkably higher in cleanliness than that of the prior art (the amount of foreign matter and fine particles attached is significantly reduced).

Claims (5)

配合・混練工程、成形工程、アルカリ洗浄処理工程、酸洗浄処理工程、温水洗浄処理工程、シャワー洗浄処理工程、乾燥処理工程、及び最終検査工程をこの順に経て、空気清浄度が段階的に高レベルとなる雰囲気下に実施する医薬・医療品用ゴム栓を製造する方法において、前記配合・混練工程を、大気をフィルターを通して、塵埃を除いた大気雰囲気中で実施し、
アルカリ洗浄処理工程、酸洗浄処理工程、温水洗浄処理工程の3つの洗浄処理工程を上記の順に1つの処理槽中で、M6.5〜M4.5の空気清浄度雰囲気下で、かつ前記温水洗浄処理工程における洗浄水は、アルカリ洗浄処理工程、及び酸洗浄処理工程における用水よりも清浄度が高い洗浄水で実施し、
該処理槽からゴム栓を取り出してシャワー洗浄処理工程に搬送し、
該シャワー洗浄処理工程以降の工程をM5.5〜M3.5の空気清浄度雰囲気下にそれぞれ実施する(但し、シャワー洗浄処理工程以降の空気清浄度は洗浄処理工程までの空気清浄度よりも高い)ことを特徴とする清浄な医薬・医療品用ゴム栓を製造する方法。
The air cleanliness is gradually increased through the blending / kneading process, molding process, alkali cleaning process, acid cleaning process, hot water cleaning process, shower cleaning process, drying process, and final inspection process in this order. In the method for producing a rubber plug for pharmaceuticals and medical products to be carried out in an atmosphere that becomes, the compounding and kneading step is carried out in an air atmosphere excluding dust through the air filter,
The three washing treatment steps of the alkali washing treatment step, the acid washing treatment step, and the hot water washing treatment step are performed in the above order in one treatment tank, under an air cleanliness atmosphere of M6.5 to M4.5, and the hot water washing. The washing water in the treatment process is performed with washing water having a higher cleanliness than the water used in the alkali washing treatment process and the acid washing treatment process ,
Remove the rubber stopper from the treatment tank and transport it to the shower cleaning process.
The steps after the shower cleaning process are carried out in an air cleanliness atmosphere of M5.5 to M3.5 (however, the air cleanliness after the shower cleaning process is higher than the air cleanliness until the cleaning process) ) A method for producing a clean rubber stopper for pharmaceuticals and medical products.
シャワー洗浄処理工程の洗浄水は、温水洗浄処理工程における洗浄水の品質と同等である請求項に記載の清浄な医薬・医療品用ゴム栓を製造する方法。The method for producing a clean rubber plug for medical / medical products according to claim 1 , wherein the washing water in the shower washing treatment step is equivalent to the quality of the washing water in the warm water washing treatment step. 成形工程以降の任意の工程で除電処理する請求項1又は2に記載の清浄な医薬・医療品用ゴム栓を製造する方法。The method for producing a clean rubber plug for a pharmaceutical or medical product according to claim 1 or 2 , wherein the static elimination treatment is performed in an arbitrary step after the molding step. 工程間のゴム栓の搬送を無人自動搬送手段による請求項1〜のいずれか1項に記載の清浄な医薬・医療品用ゴム栓を製造する方法。The method for producing a clean rubber plug for medical or medical products according to any one of claims 1 to 3 , wherein the rubber plug is conveyed between the steps by an unattended automatic conveying means. 請求項1〜のいずれか1項に記載の方法で得られる清浄な医薬・医療品用ゴム栓。Claim 1 clean pharmaceutical and medical products rubber stopper obtained by the method according to any one of 4.
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