JPS6049653B2 - Manufacturing method for synthetic resin molded products - Google Patents
Manufacturing method for synthetic resin molded productsInfo
- Publication number
- JPS6049653B2 JPS6049653B2 JP5786081A JP5786081A JPS6049653B2 JP S6049653 B2 JPS6049653 B2 JP S6049653B2 JP 5786081 A JP5786081 A JP 5786081A JP 5786081 A JP5786081 A JP 5786081A JP S6049653 B2 JPS6049653 B2 JP S6049653B2
- Authority
- JP
- Japan
- Prior art keywords
- synthetic resin
- molding
- shrinkage rate
- manufacturing
- resin molded
- 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 27
- 239000000057 synthetic resin Substances 0.000 title claims description 27
- 238000004519 manufacturing process Methods 0.000 title claims description 14
- 238000000465 moulding Methods 0.000 claims description 32
- 238000010438 heat treatment Methods 0.000 claims description 20
- 238000000034 method Methods 0.000 claims description 11
- 239000000654 additive Substances 0.000 claims description 7
- 239000004743 Polypropylene Substances 0.000 claims description 6
- 239000000945 filler Substances 0.000 claims description 6
- -1 polypropylene Polymers 0.000 claims description 6
- 229920001155 polypropylene Polymers 0.000 claims description 6
- 239000003973 paint Substances 0.000 claims description 5
- 230000000996 additive effect Effects 0.000 claims 1
- 239000000047 product Substances 0.000 description 23
- 229920005989 resin Polymers 0.000 description 12
- 239000011347 resin Substances 0.000 description 12
- 230000000052 comparative effect Effects 0.000 description 4
- 239000000463 material Substances 0.000 description 3
- 238000010422 painting Methods 0.000 description 3
- 239000002987 primer (paints) Substances 0.000 description 3
- UOCLXMDMGBRAIB-UHFFFAOYSA-N 1,1,1-trichloroethane Chemical compound CC(Cl)(Cl)Cl UOCLXMDMGBRAIB-UHFFFAOYSA-N 0.000 description 2
- 238000000576 coating method Methods 0.000 description 2
- 238000007796 conventional method Methods 0.000 description 2
- 238000001953 recrystallisation Methods 0.000 description 2
- 239000000454 talc Substances 0.000 description 2
- 229910052623 talc Inorganic materials 0.000 description 2
- 229920002943 EPDM rubber Polymers 0.000 description 1
- 239000011248 coating agent Substances 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 239000012467 final product Substances 0.000 description 1
- 239000003960 organic solvent Substances 0.000 description 1
- 238000007591 painting process Methods 0.000 description 1
- 238000006116 polymerization reaction Methods 0.000 description 1
- 229920005672 polyolefin resin Polymers 0.000 description 1
- 239000000843 powder Substances 0.000 description 1
Landscapes
- Coating Of Shaped Articles Made Of Macromolecular Substances (AREA)
- Application Of Or Painting With Fluid Materials (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、特に塗装を施さない成形品と同じ寸法を
有する塗装された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 crystalline synthetic resin, and particularly to a method for manufacturing a coated molded article having the same dimensions as an unpainted molded article. .
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、あるも
のは塗装を施さないまま使用し、またあるものは各種の
焼付塗装を施して使用している。Vehicle parts such as bumpers are molded from synthetic resins, mainly crystalline synthetic resins such as polypropylene, and some are used unpainted, while others are used with various baked-on coatings. There is.
従来の塗装を施した成形品の製造方法は、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’Cで30分間焼付し、さらに上塗塗装
をして90゜Cで和分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、成形の際に成形収縮した樹脂が焼付工程で再結
晶して熱収縮するため、塗装を施さない成形品より小形
になり、これを防ぐには別の大きな金型を使用して成形
しなければならなかつた。The conventional manufacturing method for painted molded products is to wash with an organic solvent such as trichloroethane after molding, apply a primer coat, bake at 80°C for 30 minutes, and then apply a topcoat and bake at 90°C. The image is being baked for a minute. However, in such conventional manufacturing methods for synthetic resin molded products, the resin that shrinks during molding recrystallizes and heat shrinks during the baking process, resulting in smaller products than unpainted molded products. To prevent this, it had to be molded using a separate large mold.
また焼付温度が80〜90℃であるため、熱収縮率にバ
ラツキを生じ、塗装を施した最終製品の間も寸法が一定
しないという問題点があつた。 この発明は、このよう
な従来の問題点に着目してなされたもので、所定の成形
収縮率を有する合成樹脂を使用して成形し、塗装焼付工
程に先立つて、焼付温度よりも混い温度て加熱処理し、
成形および加熱処理による全体の収縮率を、塗装を施さ
ない成形品の成形収縮率と一致させることにより、上記
問題点を解決することを目的としている。Further, since the baking temperature is 80 to 90°C, there is a problem that the heat shrinkage rate varies and the dimensions of the finished product after coating are not constant. This invention was made by focusing on these conventional problems, and involves molding using a synthetic resin having a predetermined molding shrinkage rate, and then molding the resin at a temperature lower than the baking temperature prior to the paint baking process. heat treated,
The purpose is to solve the above-mentioned problems by making the overall shrinkage rate due to molding and heat treatment match the molding shrinkage rate of a molded product that is not coated.
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、所定の成形収縮率を有する合成樹脂て成形
したのち、塗装焼付工程に先立つて、焼付温度よりも高
い温度で加熱処理し、成形および加熱処理による全体の
収縮率を、塗装を施さない成形品の成形収縮率と一致さ
せ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. A method for producing a synthetic resin molded article, characterized in that it is first heat treated at a temperature higher than the baking temperature, so that the overall shrinkage rate due to molding and heat treatment matches the molding shrinkage rate of a molded article that is not coated. It is.
従来法において熱収縮率に差が生じる原因について検討
した結果、80〜90℃の温度で、30〜4紛間焼付を
行つた場合、収縮率にバラツキを生じ、また80゜Cて
焼付を行つたのち90゜Cで再ひ焼付を行うと、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 heat shrinkage rates in conventional methods, it was found that when 30 to 4 powder baking was performed at a temperature of 80 to 90°C, the shrinkage rate varied; It was found that when the material was reheated at 90°C after the test, 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で成形した
車両用パンパー(成形収縮率1511000および14
11000のもの)について金型(長手方向の幅170
?)に対する収縮率の経時変化を加熱温度ごとに測定し
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以上で加熱
処理した場合は収縮率にバラツキがなく、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、特に高温で加
熱処理して収縮率が安定した場合には、その後さらに低
温で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、焼付温度より
も高温で、樹脂の収縮率が早期に安定する温度で加熱処
理を行うと、樹脂の再結晶化が終了して収縮率は一定と
なり、その後上記加熱処理温度より低温で焼付を行つて
も熱収縮は起らない。The drawing shows a vehicle pumper (molding shrinkage rate 1511000 and 14
11000) for the mold (longitudinal width 170
? ) is a graph showing the results of measuring the change in shrinkage rate over time for each heating temperature, and shows that the above phenomenon occurs. On the other hand, when heat-treated at 100'C or higher, there is no variation in the shrinkage rate, and the shrinkage rate becomes constant at about 30 to 6 gin, indicating that the shrinkage rate is stable. It was also found that once the material is heat-treated at a high temperature, especially when the shrinkage rate is stabilized by the heat treatment at a high temperature, no shrinkage occurs even if the material is further heat-treated at a lower temperature. The present invention makes use of this phenomenon. When heat treatment is performed at a temperature higher than the baking temperature, at which the shrinkage rate of the resin stabilizes early, the recrystallization of the resin ends and the shrinkage rate remains constant. Therefore, even if baking is performed at a temperature lower than the above heat treatment temperature, no thermal shrinkage occurs.
また結晶性合成樹脂は、フィラー等の添加物を選択する
ことにより成形収縮率(成形時の収縮率)を調節するこ
とが可能であるので、成形および加熱処理による全体の
収縮率を、塗装を施さない成形品の成形収縮率と一致す
るように、樹脂の成形収縮率を選択すれば、同じ成形用
の金型を使用して、塗装を施した成形品と塗装を施さな
い成形品の大きさを一致させることができ、塗装を施し
た成形品の寸法のバラツキもなくすことができる。すな
わち、塗装を施さない成形品よりも成形収縮率の小さい
樹脂により成形を行うと、大き目の成形品が生成するが
、これを加熱処理することにより、成形収縮率の高い樹
脂により成形を行つた、塗装を施さない成形と同じ寸法
となり、その後、加熱処理を行つた成形品に塗装焼付を
施しても熱収縮は起らないから、最終製品としては塗装
を施した成形品と施さない成形品の寸法は同じとなる。In addition, the molding shrinkage rate (shrinkage rate during molding) of crystalline synthetic resins can be adjusted by selecting additives such as fillers, so the overall shrinkage rate due to molding and heat treatment can be adjusted by controlling the overall shrinkage rate during molding and heat treatment. If you select the molding shrinkage rate of the resin to match the molding shrinkage rate of the unpainted molded part, the size of the painted molded part and the unpainted molded part can be reduced using the same mold. It is possible to match the dimensions of the coated molded product, and to eliminate variations in the dimensions of the coated molded product. In other words, if a molded product is molded with a resin that has a lower mold shrinkage than an unpainted molded product, a larger molded product will be produced, but by heat-treating this, it is possible to mold with a resin that has a higher mold shrinkage. , the dimensions are the same as the unpainted molding, and even if the heat-treated molded product is then painted and baked, no heat shrinkage will occur, so the final product can be either a painted molded product or an unpainted molded product. The dimensions will be the same.
成形品の加熱処理温度は焼付温度より高い温度で、収縮
率が早期に安定する温度であり、ポリプロピレンの場合
、90〜110℃で、30〜60分間熱処理を行うと再
結晶化は終了し、収縮率は安定する。The heat treatment temperature of the molded product is higher than the baking temperature, which is the temperature at which the shrinkage rate stabilizes early. In the case of polypropylene, recrystallization is completed when heat treatment is performed at 90 to 110°C for 30 to 60 minutes. The shrinkage rate becomes stable.
その後の塗装工程は従来法と同様であり、例えばプライ
マー塗装後、80゜Cで焼付し、上塗塗装後90℃で焼
付を行う。成形に使用する樹脂は結晶性合成樹脂を主体
とする樹脂で、結晶性合成樹脂としてはポリプロピレン
などのポリオレフィン樹脂が挙げられる。The subsequent painting process is similar to the conventional method; for example, after applying a primer, baking is performed at 80°C, and after applying a topcoat, baking is performed at 90°C. The resin used for molding is mainly a crystalline synthetic resin, and examples of the crystalline synthetic resin include polyolefin resins such as polypropylene.
樹脂の成形収縮率を調節するには、樹脂自体の重合度、
規則性等を変化させることによつても可能であるが、添
加物を混入することによつて容易に行うことができる。
添加物としては、タルク等のフィラーやEPDM等の他
の添加剤などがあり、添加物の種類および添加量等より
成形収縮率を調節可能にできる。成形品の加熱処理温度
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て適宜選定すること
がてきる。To adjust the molding shrinkage rate of the resin, the degree of polymerization of the resin itself,
This can be done by changing the regularity etc., but it can be easily done by mixing additives.
Examples of additives include fillers such as talc and other additives such as EPDM, and the molding shrinkage rate can be adjusted by adjusting the type and amount of additives. The heat treatment temperature and time for the molded article can be appropriately selected in accordance with the resin to be treated and the subsequent baking temperature within a range in which the shrinkage rate is stabilized.
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し、所定の成形収縮率を有
する合成樹脂を使用して成形し、塗装焼付工程に先立つ
て、焼付温度よりも高い温度て加熱処理し、成形および
加熱処理による全体の収縮率を、塗装を施さない成形品
の成形収縮率と一致させるようにしたため、塗装を施し
た成形品と施さない成形品の寸法を同じにすることがで
き、この場合塗装を施した成形品の寸法のバラツキをな
くすとともに、成形に使用する金型も同じものを使用て
きるなどの効果がある。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, molding is performed using a synthetic resin that is mainly composed of crystalline synthetic resin and has a predetermined molding shrinkage rate, and is heated to a temperature higher than the baking temperature prior to the paint baking process. The overall shrinkage rate due to molding and heat treatment is made to match the molding shrinkage rate of the unpainted molded product, so the dimensions of the coated molded product and the unpainted molded product are the same. In this case, it is possible to eliminate variations in the dimensions of the coated molded product, and the same mold can be used for molding.
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、フィラーとし
てタルクを混入して成形収収縮率を調節し、この樹脂に
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、1000Cで1時間加熱処理
を行つたのち、プライマー塗装を行つて80′Cで3吟
間焼付し、さらに上塗塗装を行つて90′Cて4吟間焼
付をした。Example: A synthetic resin mainly composed of polypropylene is mixed with talc as a filler to adjust the molding shrinkage rate. This resin is used to mold an automobile bumper. After cooling, the molded product is degreased and washed with trichloroethane, and then heated at 1000C for 1 After heat treatment for several hours, a primer coating was applied and baked at 80'C for 3 minutes, and a top coat was applied and baked at 90'C for 4 minutes.
各工程における金型に対する収縮率を表1に示す。また
比較例1として加熱処理を行わない場合、比較例2とし
てフィラーを混入しないて成形し塗装を行わない場合、
比較例3としてフィラーを混入しないで成形し塗装を行
つた場合の結果を併記する。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せず、塗装を施さない成形品(
比較例2)と同じ収縮率になることがわかる。Table 1 shows the shrinkage rate for the mold in each step. Also, Comparative Example 1 is a case where no heat treatment is performed, Comparative Example 2 is a case where no filler is mixed and molded and no painting is performed.
As Comparative Example 3, the results obtained when molding and painting were performed without mixing filler are also shown. From the above results, in the case of the example, the shrinkage rate becomes stable due to heat treatment, does not shrink due to subsequent baking, and the molded product without painting (
It can be seen that the shrinkage rate is the same as that of Comparative Example 2).
図面はポリプロピレンについて、加熱温度を変えて経時
の収縮率の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 the change in shrinkage rate over time of polypropylene by changing the heating temperature, and the numbers appended to the curves indicate the heating temperature.
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、所定の成形収縮率を有する合成樹脂で成形したの
ち、塗装焼付工程に先立つて、焼付温度よりも高い温度
で加熱処理し、成形おび加熱処理による全体の収縮率を
、塗装を施さない成形品の成形収縮率と一致させるとを
特徴とする合成樹脂成形品の製造方法。 2 合成樹脂の成形収縮の調節を、添加物の混入により
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 添加物はフィラーである特許請求の範囲第2項記載
の合成樹脂成形品の製造方法。 4 合成樹脂はポリプロピレンである特許請求の範囲第
1項ないし第3項のいずれに記載の合成樹脂成形品の製
造方法。 5 加熱温度は90〜110℃である特許請求の範囲第
1項ないし第4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 article, which involves molding a synthetic resin mainly composed of crystalline synthetic resin and then performing a paint baking process, Synthetic resin molding characterized by heat treatment at a temperature higher than the baking temperature prior to the paint baking process so that the overall shrinkage rate due to molding and heat treatment matches the molding shrinkage rate of a molded product that is not painted. method of manufacturing the product. 2. The method for producing a synthetic resin molded article according to claim 1, wherein the molding shrinkage of the synthetic resin is controlled by incorporating additives. 3. The method for producing a synthetic resin molded article according to claim 2, wherein the additive is a filler. 4. The method for producing a synthetic resin molded article according to any one of claims 1 to 3, wherein the synthetic resin is polypropylene. 5. The method for manufacturing a synthetic resin molded article according to any one of claims 1 to 4, wherein the heating temperature is 90 to 110°C.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP5786081A JPS6049653B2 (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 |
|---|---|---|---|
| JP5786081A JPS6049653B2 (en) | 1981-04-18 | 1981-04-18 | Manufacturing method for synthetic resin molded products |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS57172932A JPS57172932A (en) | 1982-10-25 |
| JPS6049653B2 true JPS6049653B2 (en) | 1985-11-02 |
Family
ID=13067740
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP5786081A Expired JPS6049653B2 (en) | 1981-04-18 | 1981-04-18 | Manufacturing method for synthetic resin molded products |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS6049653B2 (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH01157577A (en) * | 1987-12-14 | 1989-06-20 | Mini Pairo Denki:Kk | Semiconductor light emitting device |
| JPH0390464U (en) * | 1989-12-27 | 1991-09-13 | ||
| JPH04137772A (en) * | 1990-09-28 | 1992-05-12 | Sharp Corp | Trichromatic element and display apparatus |
| JPH04365382A (en) * | 1991-06-13 | 1992-12-17 | Toshiba Corp | Semiconductor light-emitting device and its driving method |
-
1981
- 1981-04-18 JP JP5786081A patent/JPS6049653B2/en not_active Expired
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH01157577A (en) * | 1987-12-14 | 1989-06-20 | Mini Pairo Denki:Kk | Semiconductor light emitting device |
| JPH0390464U (en) * | 1989-12-27 | 1991-09-13 | ||
| JPH04137772A (en) * | 1990-09-28 | 1992-05-12 | Sharp Corp | Trichromatic element and display apparatus |
| JPH04365382A (en) * | 1991-06-13 | 1992-12-17 | Toshiba Corp | Semiconductor light-emitting device and its driving method |
Also Published As
| Publication number | Publication date |
|---|---|
| JPS57172932A (en) | 1982-10-25 |
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