JPH0698677B2 - Blow molding simultaneous coating method - Google Patents
Blow molding simultaneous coating methodInfo
- Publication number
- JPH0698677B2 JPH0698677B2 JP5784185A JP5784185A JPH0698677B2 JP H0698677 B2 JPH0698677 B2 JP H0698677B2 JP 5784185 A JP5784185 A JP 5784185A JP 5784185 A JP5784185 A JP 5784185A JP H0698677 B2 JPH0698677 B2 JP H0698677B2
- Authority
- JP
- Japan
- Prior art keywords
- blow molding
- parison
- powder resin
- molded product
- heat
- 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
- 238000000071 blow moulding Methods 0.000 title claims description 20
- 238000000576 coating method Methods 0.000 title claims description 16
- 239000011347 resin Substances 0.000 claims description 32
- 229920005989 resin Polymers 0.000 claims description 32
- 239000000843 powder Substances 0.000 claims description 25
- 238000007664 blowing Methods 0.000 claims description 14
- 238000005507 spraying Methods 0.000 claims description 3
- 239000007789 gas Substances 0.000 description 18
- 239000011248 coating agent Substances 0.000 description 14
- 238000000034 method Methods 0.000 description 9
- 239000007921 spray Substances 0.000 description 8
- 238000001035 drying Methods 0.000 description 5
- 239000007788 liquid Substances 0.000 description 3
- 238000002844 melting Methods 0.000 description 3
- 230000008018 melting Effects 0.000 description 3
- 239000003973 paint Substances 0.000 description 3
- 238000001816 cooling Methods 0.000 description 2
- 239000000155 melt Substances 0.000 description 2
- 239000012768 molten material Substances 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 1
- 230000000717 retained effect Effects 0.000 description 1
- 230000009291 secondary effect Effects 0.000 description 1
- 238000007711 solidification Methods 0.000 description 1
- 230000008023 solidification Effects 0.000 description 1
Landscapes
- Application Of Or Painting With Fluid Materials (AREA)
- Blow-Moulding Or Thermoforming Of Plastics Or The Like (AREA)
Description
【発明の詳細な説明】 本発明は、プラスチックブロウ成形品の内面に対する他
の樹脂の被覆方法に係わる。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method of coating another resin on the inner surface of a plastic blow molding.
従来、プラスチックブロウ成形品の内面に対し、他の樹
脂を被覆する場合には、一旦ブロウ成形し、固化したそ
の成形品の内側より、液体塗料をスプレイ塗布する方法
が取られてきた。Conventionally, in the case of coating another resin on the inner surface of a plastic blow molded product, a method has been employed in which the liquid paint is spray-applied from the inside of the molded product which is once blow molded and solidified.
しかし、上述の方法においては、液体塗料の塗布作業終
了後、次工程として乾燥工程を必要とし、それには大型
の乾燥装置と、それに消費される熱エネルギ、及び作業
時間、作業員の工賃など、少なからざる経費を必要とし
たものである。本発明の動機は、上述の如き諸経費を省
き、熱エネルギを節減することにあった。However, in the above-mentioned method, after the completion of the coating operation of the liquid paint, a drying step is required as the next step, which requires a large-sized drying device, the heat energy consumed by the drying apparatus, the working time, the worker's wages, etc. It required a considerable amount of expense. The motive of the present invention was to save the above-mentioned various expenses and save heat energy.
本発明の目的は、プラスチックブロウ成形品に対する樹
脂被覆作業において、ブロウ成形と同時に、その内面に
粉体樹脂を被覆し、それによって従来の液体塗料塗布工
程及びその乾燥工程を省略し、生産効率の向上をはかる
ことにある。An object of the present invention is to perform a resin coating operation on a plastic blow molding product, at the same time as the blow molding, to coat the powder resin on the inner surface thereof, thereby omitting the conventional liquid paint coating step and its drying step, thereby improving the production efficiency. It is to improve.
本発明の要旨は、プラスチックのブロウ成形工程におい
て、予備成形されたパリソンの内面に対し、圧縮気体の
吹き込みによりパリソンが膨脹するまでの間に粉体樹脂
をスプレイ塗布し、パリソン自体の熱、膨脹中のパリソ
ン自体の熱、又はブロウ成形の完了した成形品自体の保
有する熱により、上記粉体樹脂を溶融塗着させる方法で
ある。The gist of the present invention is to spray the powder resin onto the inner surface of the pre-formed parison during the blow molding process of the plastic until the parison expands due to the blowing of the compressed gas. In this method, the powder resin is melted and applied by the heat of the parison itself or the heat of the molded product itself after the blow molding.
本発明による方法は、次の4つのタイミングがある。以
下、各例ごとに説明する。The method according to the present invention has the following four timings. Hereinafter, each example will be described.
第1のタイミング。第1A図及び第1B図を参照されたい。
ブロウ成形装置の押出機のクロスヘッドダイCDより押し
出されて、下方に漸次降下してくるパリソンPAに対し
て、その内側に粉体樹脂Pdをスプレイ用気体Asと共にノ
ズル8よりスプレイ(SP)させるものである。このよう
にして上記パリソンPAの内側全面が粉体樹脂によって適
当量塗布されつつ降下して、ある定位置に達する。それ
以降は従来の如く、両開きの状態で待機していた金型M
A,ABが閉じ、吹き込み用気体Abが吹き込んで、ブロウ成
形が行われるのである。ただしこの工程において、上記
の如くパリソンの内側に満遍なく塗布された粉体樹脂Pd
1は、パリソン自体の保有する熱により、その一部又は
全部が(粉体樹脂の溶融点、及びパリソンPA自体の保有
熱温度によって異なる)溶融し、パリソンPAの内面に膜
状となって溶融又は半溶融の状態で塗着(Pd1)する。
この溶融又は半溶融状の膜は、次に行われるパリソンの
膨脹工程においてもそれに追随して伸び、その塗膜が破
断するようなことはなく、更にブロウ成形完了後も、該
成形品自体の保有熱によって、半溶融体の部分は更に進
行して完全溶融体となり、均一厚さの塗膜として、該ブ
ロウ成形品B1の内側に塗着するのである。First timing. See Figures 1A and 1B.
With respect to the parison PA which is extruded from the cross head die CD of the extruder of the blow molding device and gradually descends downward, the powder resin Pd is sprayed (SP) from the nozzle 8 together with the spray gas As inside the parison PA. It is a thing. In this manner, the entire inner surface of the parison PA is lowered while being coated with an appropriate amount of the powder resin and reaches a certain position. After that, as in the past, the mold M has been waiting in a double-open state.
Blow molding is performed by closing A and AB and blowing the blowing gas Ab. However, in this process, the powder resin Pd evenly applied inside the parison as described above.
Part 1 melts partly or entirely (depending on the melting point of the powdered resin and the heat temperature of the parison PA itself) due to the heat of the parison itself, and melts into a film on the inner surface of the parison PA. Alternatively, apply (Pd 1 ) in a semi-molten state.
This molten or semi-molten film does not follow the expansion of the parison expansion step to be performed next, and the coating film does not break. Furthermore, even after completion of the blow molding, the molded product itself Due to the retained heat, the part of the semi-molten material further progresses to become a complete molten material, which is applied to the inside of the blow molded product B 1 as a coating film having a uniform thickness.
また、上述の如く、粉体樹脂はパリソン自体の熱、及び
膨脹過程中のパリソン自体の熱、更に膨脹完了後の成形
品自体の保有する熱を吸収するので、そのブロウ成形品
は冷却される。これはむしろ、ブロウ成形における成形
品の固化を促進せしめるものであって、派生的効果とし
てあげることができる。何故なら、元来ブロウ成形後
は、該ブロウ成形品を冷却する必要があり、そのために
吹き込み用気体Ab及び金型MA,MBを強制冷却していたも
のであるから、上述の粉体樹脂の溶融によるブロウ成形
品の冷却作用は、上記強制冷却を助長せしめるものとな
り、熱エネルギの節減にも寄与することになるのであ
る。Further, as described above, the powder resin absorbs the heat of the parison itself, the heat of the parison itself during the expansion process, and the heat of the molded product itself after completion of expansion, so that the blow molded product is cooled. . Rather, it accelerates the solidification of the molded product in blow molding and can be cited as a secondary effect. Because, originally, after blow molding, it is necessary to cool the blow molded product, and therefore the blowing gas Ab and the mold MA, MB are forcibly cooled. The cooling action of the blow-molded product due to melting promotes the forced cooling and contributes to the saving of heat energy.
第2のタイミング。第2図を参照されたい。パリソンが
降下し、金型が閉じるまでは従来と同じである。相異す
る点は、吹き込み用気体Abと同時に粉体樹脂Pdをスプレ
イ(SP2)することである。この場合には、粉体樹脂Pd
のスプレイ用気体Asの圧力を、吹き込み用気体Abよりも
大にすることが必要である。また状況によっては、粉体
樹脂Pdのスプレイ用気体Asによってブロウ成形すること
も可能であり、この場合には、吹き込み用気体Abを省略
することも出来る。何れにせよ、双方の気体の圧力バラ
ンスの調整が必要である。また、粉体樹脂のスプレイト
と同時間内、及びその前後、即ち吹き込み用気体Abの噴
出の前及び/又は後に粉体樹脂のスプレイを更に加える
ということも出来る。何れも、ブロウ成形の大きさ、塗
膜の厚さ、樹脂の熱特性などを勘案して選択することが
必要である。Second timing. See FIG. It is the same as before until the parison descends and the mold closes. The different point is that the powder resin Pd is sprayed (SP 2 ) at the same time as the blowing gas Ab. In this case, powder resin Pd
It is necessary to make the pressure of the spraying gas As higher than that of the blowing gas Ab. Depending on the situation, it is possible to perform blow molding with the spray gas As of the powder resin Pd, and in this case, the blowing gas Ab can be omitted. In any case, it is necessary to adjust the pressure balance of both gases. It is also possible to further add the spray of the powder resin within the same time as the spray of the powder resin, and before and after that, that is, before and / or after the ejection of the blowing gas Ab. In any case, it is necessary to take into consideration the size of blow molding, the thickness of the coating film, the thermal characteristics of the resin, and the like.
第3のタイミング。第3図を参照されたい。圧縮気体Ab
の吹き込みまでは従来と同様である。相異点は、ブロウ
成形後、粉体樹脂Pdをスプレイ塗布(SP3)することで
ある。本タイミングにおいては、粉体樹脂をより均一に
内面塗布することが出来る。ただし、ブロウ成形品とし
ては、前記第2のタイミングよりも若干温度が下がって
いるので、ブロウ成形品自体の熱エネルギは少なくなっ
ている。従って、高い溶融温度の粉体樹脂に対しては、
不向きと言える。Third timing. See FIG. Compressed gas Ab
It is the same as before until the blowing of. The difference is that the powder resin Pd is spray-coated (SP 3 ) after blow molding. At this timing, the powder resin can be applied more uniformly on the inner surface. However, since the temperature of the blow molded product is slightly lower than that of the second timing, the heat energy of the blow molded product itself is small. Therefore, for powder resin with high melting temperature,
It can be said that it is not suitable.
第4のタイミング。前記第2,第3のタイミングとを組み
合わせたものである。即ち、吹き込み用気体Abと同時
に、粉体樹脂Pdをスプレイし、パリソンPAの膨脹が完了
した後にも、まだ粉体樹脂Pdのスプレイ塗布を続けるも
のである。より塗膜を厚くしたいときなどに向いている
と言える。Fourth timing. This is a combination of the second and third timings. That is, the powder resin Pd is sprayed at the same time as the blowing gas Ab, and the spray application of the powder resin Pd is still continued even after the expansion of the parison PA is completed. It can be said that it is suitable when you want to make the coating film thicker.
以上、4つのタイミングについては、それぞれ一長一短
がありそれらの選択に当たっては、ブロウ成形品の樹脂
及び粉体樹脂等の熱特性、塗膜の厚さ、同成形品の大き
さ、装置サイクル、ブロウ成形装置の特性等諸条件を考
慮して決定すべきものである。There are advantages and disadvantages of each of the above four timings. When selecting them, the thermal characteristics of the resin and powder resin of the blow molded product, the thickness of the coating film, the size of the molded product, the equipment cycle, the blow molding It should be decided in consideration of various conditions such as device characteristics.
以上の如く、本発明による方法によれば、プラスチック
のブロウ成形品に対する内側の樹脂被覆作業を、ブロウ
成形と同時に、即ち一工程で行えるものであり、従来使
われてきた液体塗料の塗装工程及び乾燥工程のように二
工程にする必要がなく、またこれらの装置及び工賃は勿
論、熱資源の節減にも寄与するものである。As described above, according to the method of the present invention, the resin coating work on the inside of the blow molded product of the plastic can be performed simultaneously with the blow molding, that is, in one step. It is not necessary to use two steps like the drying step, and not only these equipment and labor cost but also contribute to the saving of heat resources.
第1A図は本発明による第1のタイミングのパリソン内面
に粉体樹脂を塗装する断面説明図 第1B図は同法による
ブロウ成形状態の断面説明図 第2図は本発明による第
2のタイミングで、吹き込み用気体と同時に粉体樹脂を
パリソン内面に塗装する断面説明図 第3図は本発明に
よる第3のタイミングで、パリソン膨脹後、その成形品
の内面に粉体樹脂を塗装する断面説明図 主要な符号の説明 5……圧縮気体の吹き込み管、7……粉体樹脂及びスプ
レイ用気体輸送管、8……ノズル、Ab……吹き込み用気
体、As……スプレイ用気体、Pd……粉体樹脂FIG. 1A is a sectional explanatory view of coating the resin powder on the inner surface of the parison at the first timing according to the present invention. FIG. 1B is a sectional explanatory view of a blow molding state according to the same method. FIG. 2 is at a second timing according to the present invention. , Cross-sectional explanatory view of coating powder resin on the inner surface of the parison simultaneously with the blowing gas. FIG. 3 is a cross-sectional explanatory view of coating the powder resin on the inner surface of the molded product after the parison expands at the third timing according to the present invention. Explanation of main symbols 5 ... Compressed gas blowing pipe, 7 ... Powder resin and spray gas transport pipe, 8 ... Nozzle, Ab ... Blowing gas, As ... Spraying gas, Pd ... Powder Body resin
───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.5 識別記号 庁内整理番号 FI 技術表示箇所 B29L 22:00 4F ─────────────────────────────────────────────────── ─── Continuation of the front page (51) Int.Cl. 5 Identification code Office reference number FI technical display location B29L 22:00 4F
Claims (1)
予備成形されたパリソンの内面に対し、圧縮気体(Ab)
の吹き込みによりパリソンが膨脹するまでの間に粉体樹
脂(Pd)をスプレイ塗布し、パリソン自体の熱、膨脹中
のパリソン自体の熱、又はブロウ成形の完了した成形品
自体の保有する熱により、上記粉体樹脂を溶融塗着させ
ることを特徴とするブロウ成形同時被覆方法。1. In a plastic blow molding process,
Compressed gas (Ab) against the inner surface of the preformed parison
By spray coating the powder resin (Pd) until the parison expands due to blowing, the heat of the parison itself, the heat of the parison itself during expansion, or the heat of the molded product itself after the blow molding, A blow molding simultaneous coating method, characterized in that the powder resin is melt-coated.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP5784185A JPH0698677B2 (en) | 1985-03-20 | 1985-03-20 | Blow molding simultaneous coating method |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP5784185A JPH0698677B2 (en) | 1985-03-20 | 1985-03-20 | Blow molding simultaneous coating method |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS61215034A JPS61215034A (en) | 1986-09-24 |
| JPH0698677B2 true JPH0698677B2 (en) | 1994-12-07 |
Family
ID=13067194
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP5784185A Expired - Lifetime JPH0698677B2 (en) | 1985-03-20 | 1985-03-20 | Blow molding simultaneous coating method |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0698677B2 (en) |
Families Citing this family (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2605838B2 (en) * | 1988-11-04 | 1997-04-30 | 凸版印刷株式会社 | Antimicrobial plastic container, device for manufacturing the same, and method for manufacturing the same |
| PL350931A1 (en) * | 2001-11-28 | 2003-06-02 | Jan Karch | Method of producing overprints on pet bottles |
| JP2013095243A (en) * | 2011-10-31 | 2013-05-20 | Nippon Plast Co Ltd | Method of manufacturing hollow molded article and air conditioning duct |
| JP6188221B2 (en) * | 2013-12-20 | 2017-08-30 | 日本プラスト株式会社 | Method and apparatus for manufacturing hollow molded body |
-
1985
- 1985-03-20 JP JP5784185A patent/JPH0698677B2/en not_active Expired - Lifetime
Also Published As
| Publication number | Publication date |
|---|---|
| JPS61215034A (en) | 1986-09-24 |
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