Deprecated: The each() function is deprecated. This message will be suppressed on further calls in /home/zhenxiangba/zhenxiangba.com/public_html/phproxy-improved-master/index.php on line 456
JPH0322895B2 - - Google Patents
[go: Go Back, main page]

JPH0322895B2 - - Google Patents

Info

Publication number
JPH0322895B2
JPH0322895B2 JP5669983A JP5669983A JPH0322895B2 JP H0322895 B2 JPH0322895 B2 JP H0322895B2 JP 5669983 A JP5669983 A JP 5669983A JP 5669983 A JP5669983 A JP 5669983A JP H0322895 B2 JPH0322895 B2 JP H0322895B2
Authority
JP
Japan
Prior art keywords
weight
parts
low
propylene
trichloroethane
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
Application number
JP5669983A
Other languages
Japanese (ja)
Other versions
JPS59179626A (en
Inventor
Tatsumi Kono
Takashi Sugimoto
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Mitsubishi Chemical Corp
Original Assignee
Mitsubishi Petrochemical Co Ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Mitsubishi Petrochemical Co Ltd filed Critical Mitsubishi Petrochemical Co Ltd
Priority to JP5669983A priority Critical patent/JPS59179626A/en
Publication of JPS59179626A publication Critical patent/JPS59179626A/en
Publication of JPH0322895B2 publication Critical patent/JPH0322895B2/ja
Granted legal-status Critical Current

Links

Landscapes

  • Application Of Or Painting With Fluid Materials (AREA)
  • Treatments Of Macromolecular Shaped Articles (AREA)

Description

【発明の詳細な説明】[Detailed description of the invention]

本発明は、塗装性良好で成形収縮が小さく、成
形品外観および機械的強度に優れたポリプロピレ
ン組成物をの塗装方法に関する。 自動車や家庭電化製品は、最近、省資源や省エ
ネルギーの目的で軽量化へ向うと共に美観の要請
もあつて、プラスチツク化が図られている。特
に、バンパーやインストルメントパネル等の自動
車部品については、車体の色調と調和させるた
め、塗装処理できることが要求されるようになつ
てきた。 プラスチツク化の材料として最も好まれるもの
にポリプロピレンおよびポリウレタンがある。ポ
リウレタンは塗装が容易であるが、生産性が低い
ので問題があり、一方のポリプロピレンは生産
性、物性では優れているが、極性が少なくて溶剤
にも難溶で膨潤もしにくいため塗装ができない欠
点を有する。 本発明は、この欠点を解消し、かつ自動車部品
や家電部品等の工業部品分野の厳しい要求性能
(特に高耐衝撃性、高剛性、成形品外観)を満た
した成形品を提供することを目的とし、特定の組
成物を特殊な洗滌処理することによつてのみこの
目的が達成されることを見い出して為されたもの
である。 すなわち本発明は、MFR14〜80g/10分の結
晶性プロピレン重合体54〜84重量部、ムーニー粘
度(ML1+4100℃)15〜90のエチレン−プロピレ
ン系共重合体ゴム32〜15重量部およびMFR0.6〜
25g/10分で密度0.94g/cm3超過の高密度ポリエ
チレン14〜1重量部を配合してなる成形体を1,
1,1−トリクロルエタンで蒸気洗滌して塗装す
ることを特徴とするポリプロピレン成形体の塗装
方法である。 本発明による製品は、上記の点に優れているの
で、特に塗装性や低温耐衝撃性の要求されるバン
パー、フエンダー、サイドパネル等の自動車外装
部材に好適であり、中でもバンパーに最適であ
る。 本発明で用いるプロピレン重合体は、MFR14
〜80g/10分、好ましくは15〜30g/10分の結晶
性のもので、プロピレンの単独重合体または過半
重量、好ましくは70モル%以上のプロピレンとエ
チレンもしくはプロピレン以外のα−オレフイン
とのブロツクまたはランダム共重合体またはこれ
らの混合物が好適であるが、これらにアクリル酸
や無水マレイン酸等の不飽和有機酸類またはスチ
レン、塩素等をグラフト変性したプロピレン重合
体もしくは酸化処理したプロピレン重合体を50重
量%以下混ぜたものであつても良い。 このMFRが14g/10分未満の場合は、成形性
が悪くて生産性が低いばかりでなく、フローマー
クが発生して成形体外観を悪化しやすい。一方、
MFR80g/10分超過のときは、低温耐衝撃性が
大巾に低下する。 また、本発明で用いるエチレン−プロピレン系
共重合体ゴムは、ムーニー粘度(ML1+4100℃)
が15〜90、好ましくは20〜75のもので、エチレン
含量20〜85モル%、好ましくは50〜80モル%のも
のが好適である。このゴムはエチレンとプロピレ
ンからなるもの(EPM)、エチレンとプロピレン
および非共役ジエンからなるもの(EPDM)の
外、これらの夫々にプロピレン以外のα−オレフ
インを共重合成分とした含むものであつてもよ
い。 ムーニー粘度が15未満のものは、成形体の塗膜
接着力が小さく、一方90超過のものでは成形品に
フローマークが発生しやすくなる。 更に、本発明で用いる高密度ポリエチレンは、
中低圧法で製造される密度が0.94g/cm3超過、好
ましくは0.95g/cm3以上のものでMFRが0.6〜25
g/10分、好ましくは3〜10g/10分のものであ
る。 密度が上記範囲より低いものは、成形体の低温
耐衝撃性と成形収縮の点で好ましくない。また、
MFRが0.6g/10分未満のものでは、成形品にフ
ローマークが発生しやすくなり、一方、25g/10
分超過のものでは、成形体の低温耐衝撃性が低下
する。 これら3成分の配合割合は、結晶性プロピレン
重合体が54〜84重量部、好ましくは63〜78重量
部、エチレン−プロピレン系共重合体ゴムが32〜
15重量部、好ましくは27〜20重量部および高密度
ポリエチレン14〜1重量部、好ましくは10〜2重
量部である。 結晶性プロピレン重合体が54重量部未満では、
成形体が柔らくなりすぎ、変形や傷付きが問題に
なり、一方、84重量部を超えると塗膜接着力が低
下し、低温耐衝撃性も悪くなる。 エチレン−プロピレン系共重合体ゴムが15重量
部未満では、成形体の塗膜密着力と低温衝撃強度
が充分でなく、また、異方性も大きくなり、反
り、変形が発生しやすくなる。一方、32重量部を
超えると弾性率が小さく、塗膜の焼付け時に垂れ
の変形を発生しやすく、また、製品表面が傷付き
やすくなり、軍手等で触れても表面が傷付き白化
する。 高密度ポリエチレンが1重量部未満では、成形
体のウエルド強度が低く、一方、14重量部を超え
ると、後の洗滌処理での光沢低下率か大きく、ま
たフローマークが発生して外観不良を起こす外、
厚肉部のヒケが顕著となる。 本発明では、上記の成分の外に必要に応じて顔
料、安定剤、造核剤、充填剤等の各種添加剤を用
いてもよい。 これらの成分を用いて成形体を得るには、先
ず、バンバリーミキサー、ロール、ブラベンダー
プラストグラフ、押出機等通常の混練機で組成物
ペレツトとし、これを射出成形、押出成形等で成
形する方法が実際的であるが、各成分をいきなり
成形機にかける、いわゆる直接成形も可能であ
る。ここで組成物を作る際の各成分の配合順序は
任意であるが、混練機は同方向回転二軸押出機が
最適であり、また成形は、射出成形が最適であ
る。なお、マスターバツチ方式を採ることもでき
る。 次に成形体を1,1,1−トリクロルエタンで
蒸発洗滌する方法は、沸騰1,1,1−トリクロ
ルエタンの入つた容器の蒸気が充満する中に成形
体を曝露する。成形体により1,1,1−トリク
ロルエタン蒸気の熱が奪われ、成形体表面で結露
し、液体の1,1,1−トリクロルエタンに相変
化し、滴下する。これにより成形体の表面洗滌が
なされる。この際、1,1,1−トリクロルエタ
ンの蒸気高さが一時的に低下するが、曝露成形体
の最上部よりも上にあることが望ましい。洗滌時
間は30秒ないし120秒がよいが、その前後も排除
するものではない。 1,1,1−トリクロルエタン蒸気洗滌の後、
極力、ほこり、手脂汗のつかない保管をし、塗装
を行なう。塗料は2コートタイプが適しており、
下塗りには成形体の接着性より高め、また上塗り
との反応接着を行なわせしめるための処方を施し
た塗料を、一方、上塗りには反応硬化により塗膜
を形成するウレタン系、アクリル系等の塗料が用
いられる。下塗り、上塗り共にスプレー塗装によ
り実施するのがよい。焼付温度は塗料成分により
80℃ないし120℃で行ない、その時間は10分ない
し30分間塗膜が反応硬化するまで行う。もちろ
ん、2コートの場合は2回焼付を行うのが望まし
い。 実施例 第1表に示す通り、結晶性プロピレン重合体
(PP)、エチレン−プロピレン共重合体ゴム
(EPM)および高密度ポリエチレン(PE)の合
計量100重量部の造核剤のパラ−第三級ブチル安
息香酸のアルミニウム塩を0.2重量部、紫外線吸
収剤のビス(2,2,6,6−テトラメチル−4
−ピペリジン)セバセート0.3重量部および30重
量%のカーボンブラツクを配合したポリプロピレ
ン3.3重量部を夫々添加しタンブラーで混合して
同方向二軸押出機にて混練押出し、樹脂組成物ペ
レツトを得た。小型射出成形機で所望のテストピ
ースを成形し、試験した。試験方法はMFRはJIS
−K6758法(230℃)、アイゾツト衝撃試験はJIS
−K7110法(−40℃、加工ノツチ入り)、曲げ弾
性率はJIS−K7203法、成形収縮率はASTM−D
−955−73(3mm厚)、また、洗滌による光沢低下
率は1,1,1−トリクロルエタン(TCE)蒸
気洗滌30秒の後に無処理状態との比較をしもの、
塗膜ピール強度はTCE洗滌後日本ビーケミカル
社の塗料R291下塗およびR263上塗をし110℃で
30分1ベーク後、1cm幅に塗膜を分割し、テンシ
ロン型試験機にて25mm/分の速度でピールした。 なお、第1表中の比較例8〜13においては、
1,1,1−トリクロルエタンで蒸気洗滌してい
ないテストピースで評価した。 結果を第1表に示す。
The present invention relates to a method for coating a polypropylene composition with good coating properties, low mold shrinkage, and excellent appearance and mechanical strength of molded products. Recently, automobiles and home appliances are becoming lighter in weight for the purpose of conserving resources and energy, as well as in response to requests for aesthetic appeal, and efforts are being made to use plastics. In particular, automobile parts such as bumpers and instrument panels are required to be painted to match the color tone of the vehicle body. The most preferred plasticizing materials are polypropylene and polyurethane. Although polyurethane is easy to paint, it has problems due to its low productivity.On the other hand, polypropylene has excellent productivity and physical properties, but has a disadvantage that it cannot be painted because it has low polarity, is poorly soluble in solvents, and does not swell easily. has. The purpose of the present invention is to eliminate this drawback and provide a molded product that satisfies the strict performance requirements (especially high impact resistance, high rigidity, and molded product appearance) in the field of industrial parts such as automobile parts and home appliance parts. It was discovered that this purpose could only be achieved by subjecting a particular composition to a special cleaning treatment. That is, the present invention uses 54 to 84 parts by weight of a crystalline propylene polymer with an MFR of 14 to 80 g/10 minutes, and 32 to 15 parts by weight of an ethylene-propylene copolymer rubber having a Mooney viscosity (ML 1+4 at 100°C) of 15 to 90. and MFR0.6~
1 molded product made by blending 14 to 1 part by weight of high-density polyethylene with a density exceeding 0.94 g/cm 3 at 25 g/10 minutes.
This is a method for coating a polypropylene molded article, which is characterized by coating after steam washing with 1,1-trichloroethane. Since the product according to the present invention is excellent in the above points, it is particularly suitable for automobile exterior parts such as bumpers, fenders, and side panels that require paintability and low-temperature impact resistance, and is particularly suitable for bumpers. The propylene polymer used in the present invention is MFR14
~80 g/10 min, preferably 15-30 g/10 min, crystalline, homopolymer of propylene or block of majority, preferably 70 mol% or more of propylene and ethylene or α-olefin other than propylene. Or a random copolymer or a mixture thereof is preferable, but propylene polymers graft-modified with unsaturated organic acids such as acrylic acid and maleic anhydride, or styrene, chlorine, etc. or oxidized propylene polymers are preferably used. It may be a mixture of less than % by weight. When this MFR is less than 14 g/10 minutes, not only is moldability poor and productivity low, but also flow marks are likely to occur and the appearance of the molded product is likely to deteriorate. on the other hand,
When MFR exceeds 80g/10 minutes, low-temperature impact resistance decreases significantly. In addition, the ethylene-propylene copolymer rubber used in the present invention has a Mooney viscosity (ML 1+4 100℃)
is preferably 15 to 90, preferably 20 to 75, and the ethylene content is 20 to 85 mol%, preferably 50 to 80 mol%. This rubber is composed of ethylene and propylene (EPM), ethylene, propylene and non-conjugated diene (EPDM), and each of these rubbers contains α-olefin other than propylene as a copolymerized component. Good too. If the Mooney viscosity is less than 15, the coating adhesion of the molded product will be low, while if it exceeds 90, flow marks will easily occur on the molded product. Furthermore, the high density polyethylene used in the present invention is
Manufactured by a medium-low pressure method with a density exceeding 0.94 g/cm 3 , preferably 0.95 g/cm 3 or more, and an MFR of 0.6 to 25
g/10 minutes, preferably 3 to 10 g/10 minutes. If the density is lower than the above range, it is not preferable in terms of low-temperature impact resistance and molding shrinkage of the molded product. Also,
If the MFR is less than 0.6 g/10 min, flow marks will easily occur on the molded product, while if the MFR is less than 0.6 g/10 min,
If the amount is exceeded, the low-temperature impact resistance of the molded article will decrease. The blending ratio of these three components is 54 to 84 parts by weight, preferably 63 to 78 parts by weight of the crystalline propylene polymer, and 32 to 84 parts by weight of the ethylene-propylene copolymer rubber.
15 parts by weight, preferably 27-20 parts by weight and high density polyethylene 14-1 parts by weight, preferably 10-2 parts by weight. If the crystalline propylene polymer is less than 54 parts by weight,
The molded product becomes too soft, causing problems such as deformation and scratching. On the other hand, if it exceeds 84 parts by weight, the coating film adhesion strength decreases and low-temperature impact resistance also deteriorates. If the amount of ethylene-propylene copolymer rubber is less than 15 parts by weight, the coating adhesion and low-temperature impact strength of the molded product will not be sufficient, and the anisotropy will also increase, making warping and deformation more likely. On the other hand, if it exceeds 32 parts by weight, the elastic modulus is low, and the coating film tends to sag and deform when baked, and the product surface is easily scratched, and even if touched with work gloves, the surface will be scratched and whitened. If the amount of high-density polyethylene is less than 1 part by weight, the weld strength of the molded product will be low, while if it exceeds 14 parts by weight, the gloss will decrease significantly during subsequent washing treatment, and flow marks will occur, resulting in poor appearance. outside,
Sink marks in thick parts become noticeable. In the present invention, in addition to the above-mentioned components, various additives such as pigments, stabilizers, nucleating agents, and fillers may be used as necessary. In order to obtain a molded product using these components, the composition is first made into pellets using a conventional kneading machine such as a Banbury mixer, roll, Brabender Plastograph, or extruder, and then molded by injection molding, extrusion molding, etc. Although this is practical, so-called direct molding, in which each component is immediately placed in a molding machine, is also possible. Although the order of blending the components in preparing the composition is arbitrary, the best kneading machine is a co-rotating twin screw extruder, and the best molding is injection molding. Note that a master batch method can also be adopted. Next, in the method of evaporative cleaning of the molded body with 1,1,1-trichloroethane, the molded body is exposed to a container containing boiling 1,1,1-trichloroethane filled with steam. The heat of the 1,1,1-trichloroethane vapor is removed by the molded body, dew condenses on the surface of the molded body, the phase changes to liquid 1,1,1-trichloroethane, and the vapor drips. This cleans the surface of the molded body. At this time, the vapor height of 1,1,1-trichloroethane temporarily decreases, but it is desirable that the vapor height be above the top of the exposed compact. The washing time is preferably 30 seconds to 120 seconds, but periods before or after that are not excluded. After 1,1,1-trichloroethane steam cleaning,
Store the item as dust-free, sweat-free as possible, and then paint it. A two-coat type paint is suitable.
For the undercoat, we use a paint that has a formulation that improves the adhesion of the molded object and allows for reactive adhesion with the topcoat, while for the topcoat, we use a urethane-based, acrylic-based paint that forms a coating film through reaction curing. is used. It is best to apply both the undercoat and topcoat by spray painting. The baking temperature depends on the paint composition.
It is carried out at 80°C to 120°C for 10 to 30 minutes until the coating film is cured. Of course, in the case of two coats, it is desirable to perform baking twice. Examples As shown in Table 1, a para-tertiary nucleating agent containing a total of 100 parts by weight of crystalline propylene polymer (PP), ethylene-propylene copolymer rubber (EPM), and high-density polyethylene (PE) 0.2 parts by weight of aluminum salt of butylbenzoic acid, bis(2,2,6,6-tetramethyl-4
0.3 parts by weight of (piperidine) sebacate and 3.3 parts by weight of polypropylene blended with 30% by weight of carbon black were added, mixed in a tumbler, and kneaded and extruded in a co-directional twin-screw extruder to obtain resin composition pellets. Desired test pieces were molded using a small injection molding machine and tested. Test method: MFR is JIS
−K6758 method (230℃), Izot impact test is JIS
-K7110 method (-40℃, processing notch), bending elastic modulus is JIS-K7203 method, molding shrinkage rate is ASTM-D
-955-73 (3mm thickness), and the gloss reduction rate due to cleaning was compared with the untreated state after 30 seconds of 1,1,1-trichloroethane (TCE) steam cleaning.
The peel strength of the paint film was measured at 110℃ after TCE washing with R291 undercoat and R263 topcoat from Nippon B Chemical Co., Ltd.
After baking for 30 minutes, the coating film was divided into 1 cm wide pieces and peeled at a speed of 25 mm/min using a Tensilon tester. In addition, in Comparative Examples 8 to 13 in Table 1,
Test pieces that were not steam-washed with 1,1,1-trichloroethane were evaluated. The results are shown in Table 1.

【表】【table】

Claims (1)

【特許請求の範囲】[Claims] 1 MFR14〜80g/10分の結晶性プロピレン重
合体54〜84重量部、ムーニー粘度(ML1+4100℃)
15〜90のエチレン−プロピレン系共重合体ゴム32
〜15重量部および密度0.94g/cm3超過かつ
MFR0.6〜25g/10分の高密度ポリエチレン14〜
1重量部を配合してなる成形体を1,1,1−ト
リクロルエタンで蒸気洗滌して塗装することを特
徴とするポリプロピレン成形体の塗装方法。
1 MFR14-80g/10min crystalline propylene polymer 54-84 parts by weight, Mooney viscosity (ML 1+4 100℃)
15-90 ethylene-propylene copolymer rubber 32
~15 parts by weight and density exceeding 0.94 g/cm 3 and
MFR0.6~25g/10min high density polyethylene 14~
1. A method for coating a polypropylene molded body, which comprises steam-washing a molded body containing 1 part by weight of 1,1,1-trichloroethane and painting the molded body.
JP5669983A 1983-03-31 1983-03-31 Painting of polypropylene molding Granted JPS59179626A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP5669983A JPS59179626A (en) 1983-03-31 1983-03-31 Painting of polypropylene molding

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP5669983A JPS59179626A (en) 1983-03-31 1983-03-31 Painting of polypropylene molding

Publications (2)

Publication Number Publication Date
JPS59179626A JPS59179626A (en) 1984-10-12
JPH0322895B2 true JPH0322895B2 (en) 1991-03-27

Family

ID=13034708

Family Applications (1)

Application Number Title Priority Date Filing Date
JP5669983A Granted JPS59179626A (en) 1983-03-31 1983-03-31 Painting of polypropylene molding

Country Status (1)

Country Link
JP (1) JPS59179626A (en)

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR970015655A (en) * 1995-09-06 1997-04-28 전성원 Polypropylene Bumper Cover Composition
KR970074852A (en) * 1996-05-06 1997-12-10 황선두 Polypropylene composite resin composition improved in low gloss
DE102011076959A1 (en) * 2011-06-06 2012-12-06 Kunststoff-Technik Scherer & Trier Gmbh & Co. Kg Process for producing an at least partially coated plastic part, plastic part and base body for its production

Also Published As

Publication number Publication date
JPS59179626A (en) 1984-10-12

Similar Documents

Publication Publication Date Title
EP0213720B1 (en) Filler-containing polypropylene resin compositions
JP3461971B2 (en) Polyolefins, polyolefin blends and elastomer-modified polyolefins, methods for producing these materials, and methods for producing polyolefin products and molded polyolefin products having enhanced surface polarity
JPS61233047A (en) Polypropylene resin composition
US6034177A (en) Propylene resin composition
JPH0475793B2 (en)
US3783012A (en) Vacuum metallized polyolefins
JPH0618940B2 (en) Thermoplastic composition and articles made therefrom
JPH0322895B2 (en)
US6075086A (en) Polypropylene resin composition and method for coating molded products of the resin composition
JPS60188453A (en) Filled resin composition
JPS6261061B2 (en)
JPH04218547A (en) Polypropylene resin composition and coating method for molding thereof
JP3175530B2 (en) Surface treatment method and coating method of polypropylene resin composition molded article and polypropylene resin coated molded article
JPS6264848A (en) Propylene homopolymer composition
JPH0639558B2 (en) Propylene polymer composition
JPS62167048A (en) Manufacture of multilayer structure
JPH0717795B2 (en) Propylene polymer composition
JPS63146950A (en) Polymer composition and molded article having improved heat-resistance and adhesivity of coating film
JPH0564660B2 (en)
JPH04261449A (en) Propylene polymer composition
JPH0329104B2 (en)
JPS6189239A (en) Polyolefin composition
JPS63118217A (en) Molding process of thermoplastic resin molding
JPH0639557B2 (en) Propylene polymer composition
JPH0347298B2 (en)