JPH0442178B2 - - Google Patents
Info
- Publication number
- JPH0442178B2 JPH0442178B2 JP59019381A JP1938184A JPH0442178B2 JP H0442178 B2 JPH0442178 B2 JP H0442178B2 JP 59019381 A JP59019381 A JP 59019381A JP 1938184 A JP1938184 A JP 1938184A JP H0442178 B2 JPH0442178 B2 JP H0442178B2
- Authority
- JP
- Japan
- Prior art keywords
- sheet
- polypropylene
- weight
- transparency
- parts
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Lifetime
Links
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C48/00—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
- B29C48/25—Component parts, details or accessories; Auxiliary operations
- B29C48/88—Thermal treatment of the stream of extruded material, e.g. cooling
- B29C48/911—Cooling
- B29C48/9135—Cooling of flat articles, e.g. using specially adapted supporting means
- B29C48/914—Cooling drums
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C48/00—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
- B29C48/03—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor characterised by the shape of the extruded material at extrusion
- B29C48/07—Flat, e.g. panels
- B29C48/08—Flat, e.g. panels flexible, e.g. films
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C48/00—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
- B29C48/25—Component parts, details or accessories; Auxiliary operations
- B29C48/88—Thermal treatment of the stream of extruded material, e.g. cooling
- B29C48/911—Cooling
- B29C48/9135—Cooling of flat articles, e.g. using specially adapted supporting means
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29K—INDEXING SCHEME ASSOCIATED WITH SUBCLASSES B29B, B29C OR B29D, RELATING TO MOULDING MATERIALS OR TO MATERIALS FOR MOULDS, REINFORCEMENTS, FILLERS OR PREFORMED PARTS, e.g. INSERTS
- B29K2023/00—Use of polyalkenes or derivatives thereof as moulding material
- B29K2023/10—Polymers of propylene
- B29K2023/12—PP, i.e. polypropylene
Landscapes
- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- Physics & Mathematics (AREA)
- Thermal Sciences (AREA)
- Extrusion Moulding Of Plastics Or The Like (AREA)
- Packages (AREA)
- Manufacture Of Macromolecular Shaped Articles (AREA)
- Processing And Handling Of Plastics And Other Materials For Molding In General (AREA)
Description
本発明は医薬品の錠剤、カプセル等の包装に使
用されているプレススルーパツク包装(以下、
PTP包装と略記する。)に適した透明性、熱成形
性、安全性に優れたポリプロピレンシートに関す
る。
従来、PTP包装には硬質塩化ビニル樹脂シー
ト(以下、塩ビシートと略記する。)が主に使用
されている。しかしながら、塩ビシートはアスピ
リン、杭生物質等の湿気により変質し易い医薬品
に対しては、その透湿度が大きすぎ、更に透湿度
の小さい、ポリ塩化ビニリデンを積層して使用さ
れ、そのため高価となる欠点がある。それ故によ
り安価で透湿度性の小さいPTP包装に適した樹
脂シートの出現が望まれている。
一方、ポリプロピレンシートはその透湿度が塩
ビシートより小さいにもかかわらず、透明性、熱
成形性に問題があり、PTP包装にはほとんど使
用されていないのが現情である。
ところでポリプロピレンシートの透明性を改良
する方法としては、ポリプロピレンにジベンジリ
デンソルビトール等の造核剤を添加する方法が、
また、熱成形性を改良する方法としては、ポリプ
ロピレンにポリエチレンをブレンドする方法が知
られているが、いずれも一長一短があり、例え
ば、前者においては成形性が悪く、後者において
は透明性が悪く、PTP包装に使用するには問題
がある。
ポリプロピレンシートの透明性と熱成形性を同
時に改良する方法としては、ポリプロピレンに水
素石油樹脂をブレンドする方法があり、この方法
によつて得られるポリプロピレンシートは、機械
的;光学的物性の上からPTP包装に適している
のであるが、この方法で得られるシートはノルマ
ルヘプタン(以下、n−HTと略記する。)溶出
量が多く、厚生省告示第20号の規準(150ppm以
下)を満足しないものが多く、実質上使用できな
いのが実情である。
本発明者らは、上記問題を解決すべく、鋭意検
討した結果、特定量の水素化石油樹脂を用い、特
定条件でシート化し、特定条件でアニールするこ
とにより、透明性、耐透湿性、熱成形性に優れ、
n−HT溶出量が厚生省告示第20号の基準を満足
するシートが安定に得られることを見出し、本発
明に到達した。
すなわち、本発明は、ポリプロピレン100重量
部に対して、水素化石油樹脂が3〜20重量部であ
るポリプロピレン樹脂組成物をチルロール温度が
70℃以上である条件でシーテイングし、次いで、
50℃以上の温度で30分以上アニールしたことを特
徴とする、プレススルーパツク包装用ポリプロピ
レンシートである。
本発明において、ポリプロピレンとしては、ホ
モポリプロピレン、プロピレンとエチレン、ブテ
ン−1等のα−オレフインとのランダム共重合体
が使用可能である。なかでも、JIS K7210の条件
14で測定したメルトフローインデツクス(以下、
MIと略記する。単位、g/10分。)が1〜4のも
のが、さらにホモポリプロピレンが透明性及び成
形性のバランス上好ましい。MIが1未満では透
明性が悪くなり、MIが4を越えると熱成形性に
べとつき、成形性が悪くなる。
本発明において使用する水素化石油樹脂とは、
芳香族炭化水素の水素化物、テルペン樹脂の水素
化物等であり、具体的にはスチレン、α−メチル
スチレン、ビニルトルエン、ビニルキシレン、プ
ロペニルベンゼン、インデン、メチルインデン、
エチルインデン等の各種の芳香族不飽和炭化水素
及び/又はテルペン類の1種又は2種以上の混合
物を主体として重合して得られる樹脂を水素化し
たものや石油の分解、改質の際に副生する沸点20
〜300℃、とくに150〜300℃の溜分を重合して得
られる樹脂を水素化したものがあげられる。本発
明において水素化石油樹脂の使用量は、その軟化
点により異なるが、ポリプロピレン100重量部に
対し、3〜20重量部、好ましくは6〜11重量部で
ある。その使用量が3重量部未満では透明性、熱
成形性の改良効果が不充分であり、逆に20重量部
を越して使用すると、熱成形性が悪くなる。
本発明において、ポリプロピレンと水素化石油
樹脂を予め、ポリプロピレン用安定剤とともに、
ヘンシエルミキサー等の公知の機械で配合し、押
出機等の公知の機械で樹脂組成物とし、次に、T
ダイ法等でシーテイングされ、さらにアニールさ
れる。
まず、シーテイングは、チルロール温度70℃以
上で行なわれ、このチルロール温度を採用するこ
とによりn−HT溶出量が驚くべき低下を示す。
チルロール温度は、70℃以上、好ましは75〜125
℃であり、70℃未満では効果が不充分で、n−
HT溶出量が多くなる。
上記で得られたシートは、アニールされ、n−
HT溶出量がさらに押えられる。アニールは、ア
ニール温度が50〜130℃好ましくは80〜125℃であ
る。50℃未満では効果が不充分である。又、アニ
ール時間は30分以上、より好ましくは60分以上で
ある。30分未満では効果が不充分である。
本発明の、PTP包装用ポリプロピレンシート
は、耐透湿性、透明性、安全性に優れ、且つ、
PTP包装時の熱成形性にも優れたシートであり、
PTP包装用の成形機にかけられ実用に供せられ
る。
なお、PTP包装とは、錠剤、カプセル等をプ
ラスチツクシートのポケツトと、それをシールす
るアルミ箔で包装する包装形態である、通常、熱
可塑性シートを熱成形し、これに錠剤、カプセル
等を自動充填し、アルミ箔でシールし、ミシン
目、スリツトを入れ、外周を打抜くまでの工程を
連続的におこなう高速自動包装機械を使用して実
施されている。
本発明の、PTP包装用ポリプロピレンシート
は熱成形時の成形性に優れており、且つ、アルミ
箔との熱接着性、打抜き性にも優れている為、偏
肉の少ない優れたPTP包装品が高速で得られる。
又、得られたPTP包装品の品質も、透明性、耐
透湿性、安全性ともに優れたものである。
以下、実施例により本発明を更に説明する。
実施例 1
ジタ−シヤリブチル−p−クレゾール0.1重量
部、ステアリン酸カルシウム0.1重量部を配合し
たMI=2のホモポリプロピレン100重量部に、軟
化点123℃の水素化石油樹脂を10重量部配合し、
ヘンシエルミキサーで混合した後、シリンダー径
40mmの押出機を使用して240℃で押出し、ペレツ
トを得た。
このペレツトをチルロール温度80℃、押出温度
240℃に設定したTダイ付きのシリンダー径40mm
の押出機でシーテイングし、巾200mm、厚さ0.25
mmのシートを得た。
次に、このシートを80℃で40分間アニールし、
PTP包装用ポリプロピレンシートを得た。
このシートを株式会社カナエ製のPTP包装機
M2000によりPTP包装を実施して成形性を評価
した。また、このシートの透明性、透湿性、n−
HT溶出量も測定した。結果を表−1に示す。
透明性はASTM−D−1003に従いヘイズを測
定し、透湿度はASTM−E−96に従い測定し、
n−HT溶出量は厚生省告示第20号に従つて測定
した。
比較例 1
実施例−1において、アニールを行なわない他
は全て実施例1と同様にしてPTP包装用ポリプ
ロピレンシートを得た。得られたシートの成形性
および諸物性を評価した。結果を表−1に示す。
実施例−2、3及び比較例−2
実施例−1において、アニールを表−1に示し
た時間行なう他は、実施例−1と同様にして、シ
ートを得た。得られたシートの諸物性及び成形性
を評価した。結果を表−1に示す。
The present invention is directed to press-through packaging (hereinafter referred to as
It is abbreviated as PTP packaging. ) Polypropylene sheet with excellent transparency, thermoformability and safety. Conventionally, rigid vinyl chloride resin sheets (hereinafter abbreviated as PVC sheets) have been mainly used for PTP packaging. However, the moisture permeability of PVC sheets is too high for pharmaceuticals that are susceptible to deterioration due to moisture, such as aspirin and biomaterials. Furthermore, they are used by laminating polyvinylidene chloride, which has a low moisture permeability, and are therefore expensive. There are drawbacks. Therefore, there is a desire for a resin sheet suitable for PTP packaging that is cheaper and has lower moisture permeability. On the other hand, although polypropylene sheets have lower moisture permeability than PVC sheets, they have problems with transparency and thermoformability, and are currently hardly used in PTP packaging. By the way, a method for improving the transparency of polypropylene sheets is to add a nucleating agent such as dibenzylidene sorbitol to polypropylene.
In addition, as a method for improving thermoformability, there is a known method of blending polyethylene with polypropylene, but each method has its advantages and disadvantages.For example, the former has poor moldability, and the latter has poor transparency. There are problems when using it for PTP packaging. One way to simultaneously improve the transparency and thermoformability of polypropylene sheets is to blend polypropylene with hydrogen petroleum resin. Although it is suitable for packaging, the sheet obtained by this method has a large amount of normal heptane (hereinafter abbreviated as n-HT) eluted and does not meet the standards (150 ppm or less) of Ministry of Health and Welfare Notification No. 20. The reality is that many of them are virtually unusable. In order to solve the above problems, the inventors of the present invention have conducted intensive studies and found that by using a specific amount of hydrogenated petroleum resin, forming it into a sheet under specific conditions, and annealing it under specific conditions, we have achieved transparency, moisture permeation resistance, and heat resistance. Excellent moldability,
It was discovered that a sheet whose n-HT elution amount satisfies the standards of Ministry of Health and Welfare Notification No. 20 can be stably obtained, and the present invention was achieved. That is, the present invention provides a polypropylene resin composition containing 3 to 20 parts by weight of hydrogenated petroleum resin based on 100 parts by weight of polypropylene at a chill roll temperature.
Sheeting at a temperature of 70°C or higher, then
This is a polypropylene sheet for press-through packaging, which is characterized by being annealed at a temperature of 50°C or higher for 30 minutes or more. In the present invention, as the polypropylene, homopolypropylene, a random copolymer of propylene and an α-olefin such as ethylene or butene-1 can be used. Among them, the conditions of JIS K7210
The melt flow index measured at 14 (hereinafter referred to as
Abbreviated as MI. Unit: g/10 minutes. ) is preferably 1 to 4, and homopolypropylene is more preferable in view of the balance between transparency and moldability. If the MI is less than 1, the transparency will be poor, and if the MI is more than 4, the thermoformability will be sticky and the moldability will be poor. The hydrogenated petroleum resin used in the present invention is
Aromatic hydrocarbon hydrides, terpene resin hydrides, etc., specifically styrene, α-methylstyrene, vinyltoluene, vinylxylene, propenylbenzene, indene, methylindene,
Hydrogenated resins obtained by polymerizing one or a mixture of two or more of various aromatic unsaturated hydrocarbons such as ethyl indene and/or terpenes, and when decomposing or reforming petroleum. By-product boiling point 20
Examples include hydrogenated resins obtained by polymerizing fractions at ~300°C, particularly 150-300°C. In the present invention, the amount of hydrogenated petroleum resin used varies depending on its softening point, but is 3 to 20 parts by weight, preferably 6 to 11 parts by weight, based on 100 parts by weight of polypropylene. If the amount used is less than 3 parts by weight, the effect of improving transparency and thermoformability will be insufficient, and if it is used in excess of 20 parts by weight, thermoformability will deteriorate. In the present invention, polypropylene and hydrogenated petroleum resin are prepared in advance together with a polypropylene stabilizer.
It is blended using a known machine such as a Henschel mixer, made into a resin composition using a known machine such as an extruder, and then T
Sheeting is performed using a die method or the like, and then annealing is performed. First, sheeting is performed at a chill roll temperature of 70°C or higher, and by employing this chill roll temperature, the amount of n-HT elution shows a surprising decrease.
Chill roll temperature is 70℃ or higher, preferably 75-125
℃, and below 70℃, the effect is insufficient and n-
The amount of HT elution increases. The sheet obtained above was annealed and n-
The amount of HT elution can be further reduced. The annealing temperature is 50 to 130°C, preferably 80 to 125°C. The effect is insufficient below 50°C. Further, the annealing time is 30 minutes or more, more preferably 60 minutes or more. If the time is less than 30 minutes, the effect is insufficient. The polypropylene sheet for PTP packaging of the present invention has excellent moisture permeability, transparency, and safety, and
This sheet also has excellent thermoformability during PTP packaging.
It is put into practical use by being put into a molding machine for PTP packaging. PTP packaging is a form of packaging in which tablets, capsules, etc. are wrapped in a plastic sheet pocket and aluminum foil to seal it. Usually, a thermoplastic sheet is thermoformed, and tablets, capsules, etc. are automatically packaged into this. The process is carried out using a high-speed automatic packaging machine that continuously performs the steps of filling, sealing with aluminum foil, making perforations and slits, and punching out the outer periphery. The polypropylene sheet for PTP packaging of the present invention has excellent moldability during thermoforming, and also has excellent thermal adhesion with aluminum foil and punching properties, so it can produce excellent PTP packaging products with less uneven thickness. Obtained at high speed.
Furthermore, the quality of the obtained PTP packaged product is excellent in terms of transparency, moisture permeability, and safety. The present invention will be further explained below with reference to Examples. Example 1 10 parts by weight of a hydrogenated petroleum resin with a softening point of 123°C was blended with 100 parts by weight of homopolypropylene of MI = 2, which was blended with 0.1 parts by weight of diterciabutyl-p-cresol and 0.1 parts by weight of calcium stearate.
After mixing with Henschel mixer, cylinder diameter
Pellets were obtained by extrusion at 240° C. using a 40 mm extruder. The pellets are chilled at a temperature of 80℃ and extruded at a temperature of 80℃.
Cylinder diameter 40mm with T die set at 240℃
Sheeted with an extruder, width 200mm, thickness 0.25mm
A sheet of mm was obtained. Next, this sheet was annealed at 80℃ for 40 minutes,
A polypropylene sheet for PTP packaging was obtained. This sheet is wrapped in a PTP packaging machine manufactured by Kanae Co., Ltd.
PTP packaging was performed using M2000 and moldability was evaluated. In addition, the transparency, moisture permeability, n-
The amount of HT elution was also measured. The results are shown in Table-1. Transparency was determined by measuring haze according to ASTM-D-1003, and moisture permeability was determined according to ASTM-E-96.
The n-HT elution amount was measured in accordance with Ministry of Health and Welfare Notification No. 20. Comparative Example 1 A polypropylene sheet for PTP packaging was obtained in the same manner as in Example 1 except that annealing was not performed. The moldability and physical properties of the obtained sheet were evaluated. The results are shown in Table-1. Examples 2 and 3 and Comparative Example 2 Sheets were obtained in the same manner as in Example 1, except that annealing was performed for the time shown in Table 1. The various physical properties and moldability of the obtained sheet were evaluated. The results are shown in Table-1.
【表】
実施例4、5及び比較例3、4
実施例−2において、アニールを表−1に示す
温度で行なう他は実施例−2と同様にして、シー
トを得た。そのシートの諸物性及び成形性を評価
した。結果を実施例−2と共に表−2に示す。[Table] Examples 4 and 5 and Comparative Examples 3 and 4 Sheets were obtained in the same manner as in Example 2, except that annealing was performed at the temperatures shown in Table 1. The various physical properties and moldability of the sheet were evaluated. The results are shown in Table 2 together with Example 2.
【表】
実施例6、7、比較例5
実施例−2において、チルロール温度を表−1
に示す温度にする他は実施例−2と同様にして、
シートを得た。得られたシートの諸物性及び成形
性を評価した。結果を実施例−2と共に表−3に
示す。[Table] Examples 6, 7, Comparative Example 5 In Example-2, the chill roll temperature is shown in Table-1.
In the same manner as in Example-2 except that the temperature shown in
Got a sheet. The various physical properties and moldability of the obtained sheet were evaluated. The results are shown in Table 3 together with Example 2.
【表】
実施例8、9及び比較例6、7
実施例−2において、水素化石油樹脂として、
表−4に示す軟化点のものを表−2に示す量使用
する他は、実施例−2と同様にしてシートを得
た。得られたシートの諸物性、成形性を評価し
た。結果を実施例−2と共に表−4に示す。[Table] Examples 8 and 9 and Comparative Examples 6 and 7 In Example-2, as hydrogenated petroleum resin,
A sheet was obtained in the same manner as in Example 2, except that the softening points shown in Table 4 were used in the amounts shown in Table 2. The various physical properties and moldability of the obtained sheet were evaluated. The results are shown in Table 4 together with Example 2.
Claims (1)
石油樹脂が3〜20重量部であるポリプロピレン樹
脂組成物を、チルロール温度70℃以上でシーテイ
ングし、次いで50〜130℃の温度で30分以上アニ
ールしたことを特徴とするプレススルーパツク包
装用ポリプロピレンシート。1. A polypropylene resin composition containing 3 to 20 parts by weight of hydrogenated petroleum resin based on 100 parts by weight of polypropylene is sheeted at a chill roll temperature of 70°C or higher, and then annealed at a temperature of 50 to 130°C for 30 minutes or more. A polypropylene sheet for press-through packaging featuring:
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP59019381A JPS60165220A (en) | 1984-02-07 | 1984-02-07 | Manufacture of polypropylene sheet for press through package |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP59019381A JPS60165220A (en) | 1984-02-07 | 1984-02-07 | Manufacture of polypropylene sheet for press through package |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS60165220A JPS60165220A (en) | 1985-08-28 |
| JPH0442178B2 true JPH0442178B2 (en) | 1992-07-10 |
Family
ID=11997731
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP59019381A Granted JPS60165220A (en) | 1984-02-07 | 1984-02-07 | Manufacture of polypropylene sheet for press through package |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS60165220A (en) |
-
1984
- 1984-02-07 JP JP59019381A patent/JPS60165220A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS60165220A (en) | 1985-08-28 |
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| EXPY | Cancellation because of completion of term |