JPS6049652B2 - Manufacturing method for synthetic resin molded products - Google Patents
Manufacturing method for synthetic resin molded productsInfo
- Publication number
- JPS6049652B2 JPS6049652B2 JP5785981A JP5785981A JPS6049652B2 JP S6049652 B2 JPS6049652 B2 JP S6049652B2 JP 5785981 A JP5785981 A JP 5785981A JP 5785981 A JP5785981 A JP 5785981A JP S6049652 B2 JPS6049652 B2 JP S6049652B2
- Authority
- JP
- Japan
- Prior art keywords
- synthetic resin
- resin molded
- manufacturing
- temperature
- molded product
- 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
Links
- 229920003002 synthetic resin Polymers 0.000 title claims description 26
- 239000000057 synthetic resin Substances 0.000 title claims description 26
- 238000004519 manufacturing process Methods 0.000 title claims description 13
- 238000010438 heat treatment Methods 0.000 claims description 14
- 238000000034 method Methods 0.000 claims description 14
- 239000004743 Polypropylene Substances 0.000 claims description 7
- 238000000465 moulding Methods 0.000 claims description 7
- -1 polypropylene Polymers 0.000 claims description 7
- 229920001155 polypropylene Polymers 0.000 claims description 7
- 239000003973 paint Substances 0.000 claims description 5
- 239000000047 product Substances 0.000 description 14
- 229920005989 resin Polymers 0.000 description 5
- 239000011347 resin Substances 0.000 description 5
- 239000002987 primer (paints) Substances 0.000 description 4
- 238000000576 coating method Methods 0.000 description 3
- 239000012467 final product Substances 0.000 description 3
- 238000001953 recrystallisation Methods 0.000 description 3
- UOCLXMDMGBRAIB-UHFFFAOYSA-N 1,1,1-trichloroethane Chemical compound CC(Cl)(Cl)Cl UOCLXMDMGBRAIB-UHFFFAOYSA-N 0.000 description 2
- 239000011248 coating agent Substances 0.000 description 2
- 238000007796 conventional method Methods 0.000 description 2
- 230000000052 comparative effect Effects 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 229920006038 crystalline resin Polymers 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 239000003960 organic solvent Substances 0.000 description 1
- 238000007591 painting process Methods 0.000 description 1
Landscapes
- Application Of Or Painting With Fluid Materials (AREA)
- Coating Of Shaped Articles Made Of Macromolecular Substances (AREA)
Description
【発明の詳細な説明】
この発明は結晶性合成樹脂を主体とする合成樹脂成形品
の製造方法、特に焼付塗膜を有する合成樹脂成形品の製
造方法に関するものである。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for manufacturing a synthetic resin molded article mainly made of a crystalline synthetic resin, and particularly to a method for manufacturing a synthetic resin molded article having a baked coating film.
バンパーなどの車両部品には、ポリプロピレンなどの結
晶性合成樹脂を主体とする合成樹脂を成形し、これに塗
装を施したものが使用されている。従来のこの種の合成
樹脂成形品の製造方法としては、成形後トリクロロエタ
ン等の有機溶媒による洗浄を行い、プライマー塗装をし
て80℃で30分間焼付し、さらに上塗塗装をして90
゜Cで4吟間焼付を行つている。しかしながら、このよ
うな従来の合成樹脂成形品の製造方法においては、成形
時に収縮した成形品が焼付工程で樹脂の再結晶化により
再び収縮し、しかも焼付温度が80〜900Cであるた
め、収縮率にバラツキを生じ、最終製品の寸法が一定し
ないという問題点があつた。BACKGROUND OF THE INVENTION Vehicle parts such as bumpers are made of synthetic resin, mainly made of crystalline synthetic resin such as polypropylene, and then painted. The conventional manufacturing method for this type of synthetic resin molded product is to wash it with an organic solvent such as trichloroethane after molding, apply a primer coat, bake it at 80°C for 30 minutes, and then apply a topcoat to give it a temperature of 90°C.
Baking was performed at °C for 4 minutes. However, in such conventional manufacturing methods for synthetic resin molded products, the molded product that has shrunk during molding shrinks again in the baking process due to recrystallization of the resin, and since the baking temperature is 80 to 900C, the shrinkage rate is low. There was a problem that the dimensions of the final product were not constant.
この発明は、このような従来の問題点に着目してなされ
るたもので、塗装焼付工程に先立つて、焼付温度よりも
高い温度で成形品を加熱処理することにより、上記問題
点を解決することとを目的としている。This invention has been made by focusing on these conventional problems, and solves the above problems by heat-treating the molded product at a temperature higher than the baking temperature prior to the paint baking process. The purpose is to.
この発明は結晶性合成樹脂を主体とする合成樹脂を成形
したのち、塗装焼付工程を行う合成樹脂成形品の製造方
法において、、塗装焼付工程に先立つて、焼付温度より
高い温度で成形品を加熱処理することを特徴とする合成
樹脂成形品の製造方’法である。This invention relates to a method for manufacturing synthetic resin molded products in which a synthetic resin mainly composed of crystalline synthetic resin is molded and then a paint baking process is performed, in which the molded product is heated at a temperature higher than the baking temperature prior to the paint baking process. This is a method for manufacturing a synthetic resin molded product, which is characterized by a process.
従来法において収縮率に差が生じる原因について検討し
た結果、80〜900Cの温度で、30−和分間焼付を
行つた場合、収縮率にバラツキを生じ、また80℃で焼
付を行つたのち90℃で再び焼付を行うと、さらに収縮
が進み、バラツキが大きくなることがわかつた。As a result of examining the causes of differences in shrinkage rates in conventional methods, it was found that when baking was performed for 30 minutes at a temperature of 80 to 900C, there was variation in shrinkage rate, and that after baking at 80℃, 90℃ It was found that when baking was performed again, the shrinkage progressed further and the variation became larger.
図面はポリプロピレンを主体とする合成樹脂て成形した
車両用パンパー(成形収縮率1511000および14
11000のもの)について、加熱温度ことに、金型(
長手方向の幅170?)に対する収縮率の経時変化を測
定した結果を示すグラフであり、上記のような現象が起
ることを示している。これに対して、100゜C以上て
加熱処理した場合は収縮時にバラツキがなく、約30〜
6吟で一定の収縮率となり、収縮率が安定することを示
している。また一度高温で加熱処理した場合、特に高温
て加熱処理して収縮率が安定した場合には、その後さら
に低温て加熱処理しても収縮が起らないこともわかつた
。本発明はこのような現象を利用するもので、ポリプロ
ピレンなどの結晶性合成樹脂を主体とする合成樹脂を成
形したのち、焼付温度より高温で、樹脂の収縮率が早期
に安定する温度、例えばポリプロピレンの場合、90〜
1100Cで加熱処理し、その後従来法と同様にプライ
マー塗装、焼付、ならびに上塗塗装、焼付を行う。The drawing shows a vehicle pumper (molding shrinkage rate 1511000 and 14
11,000), the heating temperature, especially the mold (
Longitudinal width 170? ) is a graph showing the results of measuring the change in shrinkage rate over time, and shows that the above phenomenon occurs. On the other hand, when heat treated at 100°C or higher, there is no variation during shrinkage, and the shrinkage is about 30°C
The shrinkage rate became constant after 6 gins, indicating that the shrinkage rate was stable. It was also found that once heat treatment is performed at a high temperature, especially if the shrinkage rate is stabilized by heat treatment at a high temperature, no shrinkage occurs even if the material is subsequently heat treated at a lower temperature. The present invention utilizes such a phenomenon, and after molding a synthetic resin mainly composed of crystalline synthetic resin such as polypropylene, molding is performed at a temperature higher than the baking temperature at which the shrinkage rate of the resin quickly stabilizes, such as polypropylene. In the case of 90~
Heat treatment is performed at 1100C, followed by primer coating, baking, topcoating, and baking in the same manner as in the conventional method.
上記加熱処理により、再結晶が終了し、収縮率が安定す
るのに要する時間は、例えば上記ポリプロピレンを10
0℃で加熱処理する場合は約30〜6吟てある。この時
間加熱処理することにより、樹脂の再結晶化が終了して
成形品の収縮率は一定となり、の後低温、例えはプイマ
ー塗装では80゜C、上塗塗装では90℃で焼付を行つ
ても成形品の収縮は起らない。このため最終製品の収縮
率は一定となり、寸法が一定する。なお、以上の説明に
おいては結晶性樹脂としてポリプロピレンを例示したが
、他の樹脂も本発明の対象となる。The time required for the above heat treatment to complete the recrystallization and stabilize the shrinkage rate is, for example,
In the case of heat treatment at 0°C, the temperature is about 30 to 6. By heating for this period of time, the recrystallization of the resin is completed and the shrinkage rate of the molded product becomes constant, so even if it is baked at a low temperature, for example 80°C for primer coating and 90°C for top coating. No shrinkage of the molded product occurs. Therefore, the shrinkage rate of the final product is constant and the dimensions are constant. In addition, although polypropylene was illustrated as an example of crystalline resin in the above description, other resins are also covered by the present invention.
加熱処理温度および時間は、対象となる樹脂およびその
後の焼付温度に合わせて、収縮率が安定する範囲で適宜
選定することができる。また本発明はパンパー、ラジエ
ータグリルなどの車両用部品のほか、車両用以外の用途
の成形品の製造にも適用可能である。以上説明してきた
ように、この発明によれば、結晶性合成樹脂を主体とす
る合成樹脂を成形したのち、塗装工程に先立つて、焼付
温度よりも高い温度て成形品を加熱処理するようにした
のて、成形品の収縮率を一定とすることができ、その後
の塗装工程では収縮が起らないため、最終製品の寸法を
一定にすることができる。The heat treatment temperature and time can be appropriately selected in accordance with the target resin and the subsequent baking temperature within a range that stabilizes the shrinkage rate. Further, the present invention is applicable to the production of vehicle parts such as bumpers and radiator grilles, as well as molded products for uses other than vehicles. As explained above, according to the present invention, after molding a synthetic resin mainly composed of crystalline synthetic resin, the molded product is heat-treated at a temperature higher than the baking temperature prior to the painting process. After that, the shrinkage rate of the molded product can be kept constant, and since no shrinkage occurs in the subsequent coating process, the dimensions of the final product can be kept constant.
次に本発明の実施例について説明する。Next, examples of the present invention will be described.
実施例
ポリプロピレンを主体とする合成樹脂により自動車用パ
ンパーを成形し、成形品を冷却後トリクロロエタンで脱
脂洗浄し、100℃で1時間加熱処理を行つたのち、プ
ライマー塗装を行なつて80゜Cで3吟間焼付し、さら
に上塗塗装を行なつて90゜Cで4紛間焼付をした。Example A bumper for an automobile was molded from a synthetic resin mainly composed of polypropylene. After cooling, the molded product was degreased and washed with trichloroethane, heat treated at 100°C for 1 hour, and then coated with a primer and heated at 80°C. It was baked for 3 minutes, then top coated and baked for 4 times at 90°C.
各工程における金型に対する収縮率を表1に示す。また
加熱処理を行なわなかつた場合の結果を比較例として併
記する。以上の結果より、実施例の場合は加熱処理によ
ソー定の収縮率となつて安定し、その後の焼付によつて
収縮しないことがわかる。Table 1 shows the shrinkage rate for the mold in each step. The results obtained without heat treatment are also shown as comparative examples. From the above results, it can be seen that in the case of the example, the shrinkage rate becomes stable due to the heat treatment and does not shrink due to subsequent baking.
図面はポリプロピレンを主体とする合成樹脂成形品につ
いて、加熱温度ごとに、金型に対する収縮率の経時変化
を測定した結果を示すグラフであり、曲線に付記した数
字は加熱温度を示す。The drawing is a graph showing the results of measuring changes over time in the shrinkage rate of a mold for each heating temperature for a synthetic resin molded product mainly made of polypropylene, and the numbers appended to the curves indicate the heating temperatures.
Claims (1)
ち、塗装焼付工程を行う合成樹脂成形品の製造方法にお
いて、塗装焼付工程に先立つて、焼付温度よりも高い温
度で成形品を加熱処理することを特徴とする合成樹脂成
形品の製造方法。 2 加熱処理は成形品の収縮率は安定するまで行うよう
にした特許請求の範囲第1項記載の合成樹脂成形品の製
造方法。 3 合成樹脂はポリプロピレンを主体とするものである
特許請求の範囲第1項または第2項記載の合成樹脂成形
品の製造方法。 4 加熱温度は90〜110℃である特許請求の範囲第
1項ないし第3項のいずれかに記載の合成樹脂成形品の
製造方法。[Scope of Claims] 1. In a method for manufacturing a synthetic resin molded product, which involves molding a synthetic resin mainly composed of crystalline synthetic resin and then performing a paint baking process, the process is performed at a temperature higher than the baking temperature prior to the paint baking process. A method for producing a synthetic resin molded product, which comprises heat-treating the molded product. 2. The method for producing a synthetic resin molded article according to claim 1, wherein the heat treatment is performed until the shrinkage rate of the molded article is stabilized. 3. The method for producing a synthetic resin molded article according to claim 1 or 2, wherein the synthetic resin is mainly polypropylene. 4. The method for manufacturing a synthetic resin molded article according to any one of claims 1 to 3, wherein the heating temperature is 90 to 110°C.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP5785981A JPS6049652B2 (en) | 1981-04-18 | 1981-04-18 | Manufacturing method for synthetic resin molded products |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP5785981A JPS6049652B2 (en) | 1981-04-18 | 1981-04-18 | Manufacturing method for synthetic resin molded products |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS57172931A JPS57172931A (en) | 1982-10-25 |
| JPS6049652B2 true JPS6049652B2 (en) | 1985-11-02 |
Family
ID=13067711
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP5785981A Expired JPS6049652B2 (en) | 1981-04-18 | 1981-04-18 | Manufacturing method for synthetic resin molded products |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS6049652B2 (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH0367462U (en) * | 1989-10-31 | 1991-07-01 | ||
| JPH05251749A (en) * | 1992-03-04 | 1993-09-28 | Sharp Corp | Full color led lamp |
-
1981
- 1981-04-18 JP JP5785981A patent/JPS6049652B2/en not_active Expired
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH0367462U (en) * | 1989-10-31 | 1991-07-01 | ||
| JPH05251749A (en) * | 1992-03-04 | 1993-09-28 | Sharp Corp | Full color led lamp |
Also Published As
| Publication number | Publication date |
|---|---|
| JPS57172931A (en) | 1982-10-25 |
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