JPH06304942A - Production of deep draw press molded product - Google Patents

Production of deep draw press molded product

Info

Publication number
JPH06304942A
JPH06304942A JP9447193A JP9447193A JPH06304942A JP H06304942 A JPH06304942 A JP H06304942A JP 9447193 A JP9447193 A JP 9447193A JP 9447193 A JP9447193 A JP 9447193A JP H06304942 A JPH06304942 A JP H06304942A
Authority
JP
Japan
Prior art keywords
thermosetting resin
mold
time
molded product
resin composition
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.)
Pending
Application number
JP9447193A
Other languages
Japanese (ja)
Inventor
Norihito Morishima
憲仁 森島
Takeshi Muranaka
健 村中
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.)
Sekisui Chemical Co Ltd
Original Assignee
Sekisui Chemical 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 Sekisui Chemical Co Ltd filed Critical Sekisui Chemical Co Ltd
Priority to JP9447193A priority Critical patent/JPH06304942A/en
Publication of JPH06304942A publication Critical patent/JPH06304942A/en
Pending legal-status Critical Current

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  • Casting Or Compression Moulding Of Plastics Or The Like (AREA)

Abstract

PURPOSE:To efficiently produce a deep draw press molded product excellent in the surface gloss or smoothness in its rising surface in large quantities from a thermosetting resin compsn. by a thermal press molding method. CONSTITUTION:When a thermosetting resin compsn. is supplied to a mold consisting of upper and lower molds to produce a molded product having a deep draw shape by thermal press molding, the mold is vibrated within a time range of Tv represented by formula Tk+(Tp-Tk)/2>=Tv>=Tp+(Tp-Tk) (wherein Tk is the time up to a kick-off point starting the sudden generation of curing heat of the thermosetting resin compsn. from a point of time when the thermosetting resin compsn. comes into contact with both surfaces of the upper and lower molds and Tp is the time up to the max. generation of heat) from the point of time when the thermosetting resin compsn. comes into contact with the surfaces of the upper and lower molds in a thermal press molding process.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は、深絞りプレス成形品の
製造方法に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for producing a deep-draw press-formed product.

【0002】[0002]

【従来の技術】熱硬化性樹脂をマトリックス樹脂とし、
充填剤、骨材、硬化触媒、内部離型剤、顔料からなる熱
硬化性樹脂組成物を用いて、成形品を大量かつ比較的安
価に製造する方法として、シートモールディングコンパ
ウンド(SMC)やバルクモールディングコンパウンド
(BMC)等の成形材料を加熱プレス成形する方法が挙
げられる。
2. Description of the Related Art A thermosetting resin is used as a matrix resin,
Sheet molding compound (SMC) or bulk molding is used as a method for manufacturing a large amount of molded products at a relatively low cost using a thermosetting resin composition including a filler, an aggregate, a curing catalyst, an internal mold release agent, and a pigment. A method of hot press molding a molding material such as a compound (BMC) can be mentioned.

【0003】上記成形材料の加熱プレス成形法により、
浴槽のような立ち上がり面を有する成形品を成形する場
合、硬化時の成形収縮等により立ち上がり面が変形し
て、表面に微小な凹凸を生じることにより成形材料と金
型面と十分に接触せず、十分な圧力が加わらないため、
立ち上がり面の平滑不良や光沢不良を起こすという問題
点があった。特に肉厚の厚い成形品の場合にこの傾向が
顕著になる。
By the hot press molding method of the above molding material,
When molding a molded product with a rising surface such as a bathtub, the rising surface is deformed due to molding shrinkage during curing, etc., and minute irregularities are generated on the surface, so the molding material and the mold surface do not contact sufficiently. , Because not enough pressure is applied,
There was a problem that the rising surface had poor smoothness and poor gloss. This tendency becomes remarkable especially in the case of a thick molded product.

【0004】この対策として、成形材料に低収縮剤を多
量に添加して、成形収縮を小さくする方法が行われてい
るが、熱硬化性樹脂の硬化収縮に比べて、低収縮剤の熱
膨張が遅れて起こるため、熱硬化性樹脂と金型面が十分
に接触せず、外観の悪い成形品しか得られないという問
題点があった。
As a countermeasure against this, a method of adding a large amount of a low-shrinking agent to a molding material to reduce the molding shrinkage has been carried out. However, the thermal expansion of the low-shrinking agent is higher than that of the thermosetting resin. However, there is a problem in that the thermosetting resin and the mold surface do not come into sufficient contact with each other and only a molded product having a poor appearance can be obtained.

【0005】また、外観の良好な成形品を得るために、
振動プレス機による成形方法が特開平3−24919号
公報が開示されているが、振動によって金型面と成形品
との間に表面摩擦を起こすため、成形品の立ち上がり面
の表面平滑性が得られ難いという問題点があった。
Further, in order to obtain a molded product having a good appearance,
Japanese Patent Laid-Open No. 3-24919 discloses a molding method using a vibration press machine. However, vibration causes a surface friction between the mold surface and the molded product, so that the surface smoothness of the rising surface of the molded product is obtained. There was a problem that it was difficult to be done.

【0006】[0006]

【発明が解決しようとする課題】本発明は、上記問題点
に鑑みてなされたものであり、その目的は、加熱プレス
成形法により、立ち上がり面において、表面の平滑性や
光沢に優れた熱硬化性樹脂組成物の深絞りプレス成形品
を、大量に効率よく製造する方法を提供することにあ
る。
SUMMARY OF THE INVENTION The present invention has been made in view of the above problems, and an object of the present invention is to obtain a thermosetting material having excellent surface smoothness and gloss on the rising surface by a hot press molding method. It is an object of the present invention to provide a method for efficiently producing a deep-drawing press-formed product of a water-soluble resin composition in a large amount.

【0007】[0007]

【課題を解決するための手段】本発明で用いられる熱硬
化性樹脂組成物は、熱硬化性樹脂及び補強材からなる。
The thermosetting resin composition used in the present invention comprises a thermosetting resin and a reinforcing material.

【0008】上記熱硬化性樹脂としては、例えば、不飽
和ポリエステル樹脂、ビニルエステル樹脂等、従来公知
のものが挙げられる。
Examples of the thermosetting resin include conventionally known resins such as unsaturated polyester resin and vinyl ester resin.

【0009】上記不飽和ポリエステル樹脂は、酸成分と
多価アルコール成分とを反応させて得られる不飽和ポリ
エステルを、重合性単量体に溶解させたものが好まし
い。上記酸成分としては、α、β−不飽和二塩基酸及び
その無水物が挙げられ、これらは単独で使用されてもよ
く、2種以上が併用されてもよい。
The unsaturated polyester resin is preferably one in which an unsaturated polyester obtained by reacting an acid component and a polyhydric alcohol component is dissolved in a polymerizable monomer. Examples of the acid component include α, β-unsaturated dibasic acids and anhydrides thereof, and these may be used alone or in combination of two or more.

【0010】上記α、β−不飽和二塩基酸としては、例
えば、マレイン酸、フマル酸、イタコン酸、ジトラコン
酸、クロルマレイン酸等が挙げられ、これらは単独で使
用されてもよく、2種以上が併用されてもよい。
Examples of the α, β-unsaturated dibasic acid include maleic acid, fumaric acid, itaconic acid, ditraconic acid and chloromaleic acid, which may be used alone or in combination of two kinds. The above may be used in combination.

【0011】上記多価アルコールとしては、例えば、エ
チレングリコール、ジエチレングリコール、プロピレン
グリコール、ジプロピレングリコール、1,3−ブタン
ジオール、ネオペンチルグリコール、1,6−ヘキサン
ジオール、トリエチレングリコール、水素添加ビスフェ
ノールA、イソペンチルグリコール、グリセリン、トリ
メチロールプロパン、ジシクロペンタジエン等が挙げら
れる。
Examples of the polyhydric alcohol include ethylene glycol, diethylene glycol, propylene glycol, dipropylene glycol, 1,3-butanediol, neopentyl glycol, 1,6-hexanediol, triethylene glycol, hydrogenated bisphenol A. , Isopentyl glycol, glycerin, trimethylolpropane, dicyclopentadiene and the like.

【0012】上記酸成分には、必要に応じて、飽和二塩
基酸及びその無水物のうち少なくともいずれか1種が添
加されてもよい。
At least one kind of saturated dibasic acid and its anhydride may be added to the above acid component, if necessary.

【0013】上記飽和二塩基酸としては、例えば、フタ
ル酸、イソフタル酸、テレフタル酸、トリメリット酸、
コハク酸、アゼライン酸、アジピン酸、テトラヒドロフ
タル酸、ヘキサヒドロフタル酸、クロレンディック酸、
テトラクロロフタル酸、テトラブロモフタル酸等が挙げ
られる。
Examples of the saturated dibasic acid include phthalic acid, isophthalic acid, terephthalic acid, trimellitic acid,
Succinic acid, azelaic acid, adipic acid, tetrahydrophthalic acid, hexahydrophthalic acid, chlorendic acid,
Examples thereof include tetrachlorophthalic acid and tetrabromophthalic acid.

【0014】上記重合性単量体としては、例えば、スチ
レン、ビニルトルエン、ジビニルベンゼン、α−メチル
スチレン、クロルスチレン、ジクロルスチレン、酢酸ビ
ニル、ジアリルフタレート、ジアリルイソフタレート、
ジアリルテレフタレート等の不飽和ポリエステルと架橋
可能なビニルモノマー、ビニルオリゴマー等が挙げられ
るが、一般的にはスチレンが使用される。
Examples of the polymerizable monomer include styrene, vinyltoluene, divinylbenzene, α-methylstyrene, chlorostyrene, dichlorostyrene, vinyl acetate, diallyl phthalate, diallyl isophthalate,
Examples thereof include vinyl monomers and vinyl oligomers that can be crosslinked with unsaturated polyesters such as diallyl terephthalate, but styrene is generally used.

【0015】上記ビニルエステル樹脂としては、エステ
ル連鎖又はエーテル連鎖の末端にビニル基を有するもの
であり、一般的にはエポキシアクリレートが挙げられ
る。
The above-mentioned vinyl ester resin has a vinyl group at the terminal of the ester chain or ether chain, and generally includes epoxy acrylate.

【0016】上記不飽和ポリエステル樹脂中、不飽和ポ
リエステルの量は少なくなると十分な強度を持った成形
品が得られなくなり、多くなると成形性及び作業性が悪
くなるので、不飽和ポリエステル樹脂100重量部中、
不飽和ポリエステル50〜80重量部に対して、重合性
単量体50〜20重量部の割合で混合されているのが好
ましい。
In the unsaturated polyester resin, if the amount of unsaturated polyester is small, a molded product having sufficient strength cannot be obtained, and if it is large, moldability and workability are deteriorated. Therefore, 100 parts by weight of unsaturated polyester resin is used. During,
It is preferable that 50 to 20 parts by weight of the polymerizable polyester is mixed with 50 to 80 parts by weight of the unsaturated polyester.

【0017】上記補強材としては、例えば、ガラス繊
維;ポリエステル、フェノール、ビニロン等の合成繊
維;カーボン繊維等が挙げられるが、一般的にはガラス
繊維が使用される。上記補強材の添加量は成形体の強
度、粘度等を考慮して適宜決定される。
Examples of the reinforcing material include glass fibers; synthetic fibers such as polyester, phenol and vinylon; carbon fibers and the like, but glass fibers are generally used. The amount of the reinforcing material added is appropriately determined in consideration of the strength and viscosity of the molded product.

【0018】上記熱硬化性樹脂組成物には、さらに必要
に応じて、従来公知の硬化触媒、充填剤、低収縮剤、内
部離型剤、増粘剤、補強材、顔料等が適宜添加されても
よい。
If necessary, conventionally known curing catalysts, fillers, low-shrinking agents, internal mold release agents, thickeners, reinforcing materials, pigments and the like are appropriately added to the thermosetting resin composition. May be.

【0019】上記不飽和ポリエステル樹脂に用いられる
硬化触媒としては、例えば、t−ブチルパーオキシベン
ゾエート、ベンゾイルパーオキサイド、メチルエチルケ
トンパーオキサイド、t−ブチルパーオキシイソプロピ
ルカーボネート、t−ブチルパーオキシ−2−エチルヘ
キサノエート、1,1−ジ−t−ブチルパーオキシシク
ロヘキサノン等の有機過酸化物を挙げられる。
Examples of the curing catalyst used for the above unsaturated polyester resin include t-butylperoxybenzoate, benzoyl peroxide, methyl ethyl ketone peroxide, t-butyl peroxyisopropyl carbonate and t-butyl peroxy-2-ethyl. Examples thereof include organic peroxides such as hexanoate and 1,1-di-t-butylperoxycyclohexanone.

【0020】上記硬化触媒の量は、不飽和ポリエステル
樹脂100重量部に対して0.5〜3重量部が好まし
い。
The amount of the above curing catalyst is preferably 0.5 to 3 parts by weight with respect to 100 parts by weight of the unsaturated polyester resin.

【0021】上記充填剤としては、例えば、炭酸カルシ
ウム、炭酸マグネシウム、硫酸バリウム、タルク、クレ
ー、マイカ、シリカ、アルミナ、ガラス粉、水酸化アル
ミニウム、水酸化マグネシウム、寒水石、珪砂、樹脂粉
砕片、ゲルコートチップ等が挙げられる。特に、硬化時
の透明感を得るためには、水酸化アルミニウムが好まし
い。
Examples of the above-mentioned filler include calcium carbonate, magnesium carbonate, barium sulfate, talc, clay, mica, silica, alumina, glass powder, aluminum hydroxide, magnesium hydroxide, cold water stone, silica sand, crushed resin pieces, Examples thereof include gel-coated chips. In particular, aluminum hydroxide is preferable in order to obtain a transparent feeling upon curing.

【0022】上記充填剤の添加量は、一般に経済性、作
業性、成形体の強度等を考慮して決められるが、細密充
填となるような量が好ましい。
The amount of the above-mentioned filler to be added is generally determined in consideration of economical efficiency, workability, strength of the molded product, etc., but it is preferable that the amount be a close packing.

【0023】上記低収縮剤としては、例えば、ポリエチ
レン、ポリスチレン、ポリメタクリル酸メチル、ポリ塩
化ビニル、ポリ酢酸ビニル、ポリカプロラクタム、飽和
ポリエステル等の熱可塑性樹脂;ポリブタジエンゴム;
ポリスチレン−アクリロニトリル共重合体が挙げられ
る。
Examples of the low-shrinking agent include thermoplastic resins such as polyethylene, polystyrene, polymethylmethacrylate, polyvinyl chloride, polyvinyl acetate, polycaprolactam and saturated polyester; polybutadiene rubber;
A polystyrene-acrylonitrile copolymer is mentioned.

【0024】上記内部離型剤としては、例えば、ステア
リン酸、ステアリン酸亜鉛、ステアリン酸エステル、ア
ルキルリン酸エステル等が挙げられる。上記内部離型剤
の添加量は不飽和ポリエステル樹脂100重量部に対し
て0.5〜10重量部が好ましい。
Examples of the internal release agent include stearic acid, zinc stearate, stearic acid ester, alkyl phosphoric acid ester and the like. The amount of the internal release agent added is preferably 0.5 to 10 parts by weight with respect to 100 parts by weight of the unsaturated polyester resin.

【0025】上記増粘剤としては、例えば、不飽和ポリ
エステルが有する水酸基、カルボキシル基及びエステル
結合と化学的に結合して、線状又は一部交叉結合を生じ
て分子量を増大させ不飽和ポリエステル樹脂を増粘する
性質を有するものであり、例えば、トルイレンジイソシ
アネートなどのジイソシアネート類;アルミニウムイソ
プロポキシド、チタンテトラブトキシド等の金属アルコ
キシド類;酸化マグネシウム、酸化カルシウム、酸化ベ
リリウム等の二価金属の酸化物類;水酸化カルシウム等
の二価金属の水酸化物類が挙げられる。
Examples of the above-mentioned thickening agent include unsaturated polyester resins which chemically bond with the hydroxyl group, carboxyl group and ester bond of the unsaturated polyester to form a linear or partial crosslinkage to increase the molecular weight. For example, diisocyanates such as toluylene diisocyanate; metal alkoxides such as aluminum isopropoxide and titanium tetrabutoxide; oxidation of divalent metals such as magnesium oxide, calcium oxide and beryllium oxide. Substances: Divalent metal hydroxides such as calcium hydroxide can be mentioned.

【0026】上記増粘剤の添加量は不飽和ポリエステル
樹脂100重量部に対して0.5〜10重量部が好まし
い。
The amount of the thickener added is preferably 0.5 to 10 parts by weight with respect to 100 parts by weight of the unsaturated polyester resin.

【0027】上記顔料としては、熱硬化性樹脂の硬化性
を著しく阻害しないものであれば、特に限定されない。
The pigment is not particularly limited as long as it does not significantly impair the curability of the thermosetting resin.

【0028】上記熱硬化性樹脂組成物は、従来公知のモ
ルタルミキサー、ニーダー等の混練機を用いて混練する
ことにより、バルクモールディングコンパウンド(BM
C)やシートモールディングコンパウンド(SMC)等
の成形材料に容易に調製することができる。
The thermosetting resin composition is kneaded using a kneader such as a conventionally known mortar mixer or kneader to obtain a bulk molding compound (BM).
It can be easily prepared into a molding material such as C) or sheet molding compound (SMC).

【0029】上記熱硬化性樹脂組成物から揮発性成分が
蒸発するのを防止するために、該熱硬化性樹脂組成物を
ポリエチレンラミネートセロハン等で包み、常温又は加
熱による熟成により増粘する。この増粘により、熱硬化
性樹脂組成物は比較的硬い粘土状を呈し、冷暗所で塊状
物又は板状物として長期間にわたって安定に貯蔵できる
ようになる。
In order to prevent the volatile components from evaporating from the thermosetting resin composition, the thermosetting resin composition is wrapped in polyethylene laminated cellophane or the like and thickened by aging at room temperature or by heating. Due to this thickening, the thermosetting resin composition has a relatively hard clay-like shape and can be stably stored as a lump or a plate in a cool dark place for a long period of time.

【0030】上記増粘の方法としては、常温の場合は2
4〜72時間静置するだけでよく、加熱する場合は熱硬
化性樹脂組成物のライフが損なわれない温度、例えば、
35〜60℃での熟成が挙げられる。
The above-mentioned thickening method is 2 at room temperature.
It is enough to stand for 4 to 72 hours, and when heated, a temperature at which the life of the thermosetting resin composition is not impaired, for example,
Examples include aging at 35 to 60 ° C.

【0031】本発明では、上記熱硬化性樹脂組成物を上
型及び下型からなる深絞り用金型に供給して加熱プレス
成形する際に、金型を一定時間振動させる。上記加熱プ
レス成形の条件としては、温度が90〜170℃、圧力
が成形品の投影面積に対して10〜150kgf/cm
2 が好ましい。
In the present invention, when the thermosetting resin composition is supplied to a deep drawing die consisting of an upper die and a lower die for hot press molding, the die is vibrated for a certain period of time. The conditions for the above heat press molding are a temperature of 90 to 170 ° C. and a pressure of 10 to 150 kgf / cm with respect to the projected area of the molded product.
2 is preferred.

【0032】上記加熱プレス成形において、金型を振動
させる時点が早すぎると、熱硬化性樹脂組成物の硬化が
不十分となり、また遅くなりすぎると熱硬化性樹脂組成
物の硬化が完了するため、いずれの場合も本発明の効果
が得られないので、金型を振動させる時間範囲は下式T
vで表される。
In the above heat press molding, if the time at which the mold is vibrated is too early, the thermosetting resin composition will be insufficiently cured, and if it is too late, the thermosetting resin composition will be completely cured. In any case, since the effect of the present invention cannot be obtained, the time range for vibrating the mold is represented by the following formula T
It is represented by v.

【0033】 Tk+(Tp−Tk)/2≦Tv≦Tp+(Tp−Tk)Tk + (Tp−Tk) / 2 ≦ Tv ≦ Tp + (Tp−Tk)

【0034】式中、Tkは、熱硬化性樹脂組成物が上型
及び下型の両面に接触した時間を起点として、該樹脂組
成物が急激に硬化発熱を開始するキックオフ点までの時
間を示し、Tpは、該樹脂組成物が上型及び下型の両面
に接触した時間を起点として最高発熱を示すまでの時間
を示す。
In the formula, Tk represents the time from the time when the thermosetting resin composition comes into contact with both surfaces of the upper mold and the lower mold to the kick-off point at which the resin composition suddenly starts heat generation for curing. , Tp represents the time until the maximum heat generation starts from the time when the resin composition contacts both surfaces of the upper mold and the lower mold.

【0035】上記Tvの時間範囲では、熱硬化性樹脂組
成物の硬化が進行して、半硬化もしくは略完全硬化の状
態になるが、流動性を保持しているので、金型を振動さ
せながら加熱プレス成形することにより、熱硬化性樹脂
組成物と金型が接触して、外観が良好で光沢のある成形
品が得られる。
Within the time range of Tv, the thermosetting resin composition is cured to become a semi-cured or almost completely cured state, but since the fluidity is maintained, the mold is vibrated while being vibrated. By heat press molding, the thermosetting resin composition and the mold are brought into contact with each other, and a molded article having a good appearance and gloss can be obtained.

【0036】上記金型の振動は上下左右の三次元方向が
好ましく、金型を振動させる方法としては、例えば、カ
ムクランク方式、アンバランスエウィト方式等の機械的
方式;動電型加振機等の電磁型の電気方式;電気油圧方
式等が挙げられる。
Vibration of the mold is preferably in the three-dimensional directions of up, down, left and right. As a method of vibrating the mold, for example, a mechanical system such as a cam crank system or an unbalanced ewet system; an electrodynamic exciter. Electromagnetic type electric system such as electro-hydraulic system.

【0037】上記熱硬化性樹脂組成物のキックオフ点及
び最高発熱を示すまでの時間は、あらかじめ温度センサ
ーにより実測しておく方が好ましい。
It is preferable that the kick-off point of the above-mentioned thermosetting resin composition and the time until it exhibits the maximum heat generation are measured in advance by a temperature sensor.

【0038】[0038]

【実施例】以下に、本発明の実施例を説明する。 (実施例1〜3、比較例1〜5)フマル酸、イソフタル
酸及びプロピレグリコールからなる不飽和ポリエステル
成分と、スチレンモノマー及びポリスチレンを重合性単
量体とする不飽和ポリエステル樹脂100重量部、酸化
マグネシウム1重量部、硬化剤t−ブチルパーオキシベ
ンゾエート1重量部、ステアリン酸亜鉛5重量部ならび
に水酸化アルミニウム200重量部からなる熱硬化性樹
脂組成物を、1/2インチのチョップドガラス繊維34
重量部に含浸させ、40℃にて24時間熟成してシート
モールディングコンパウンド(SMC)を得た。
EXAMPLES Examples of the present invention will be described below. (Examples 1 to 3, Comparative Examples 1 to 5) Unsaturated polyester component consisting of fumaric acid, isophthalic acid and propylene glycol, and 100 parts by weight of unsaturated polyester resin containing styrene monomer and polystyrene as polymerizable monomers, A thermosetting resin composition containing 1 part by weight of magnesium oxide, 1 part by weight of a curing agent of t-butylperoxybenzoate, 5 parts by weight of zinc stearate and 200 parts by weight of aluminum hydroxide was mixed with 1/2 inch chopped glass fiber 34.
A part by weight was impregnated and aged at 40 ° C. for 24 hours to obtain a sheet molding compound (SMC).

【0039】上記SMCを使用し、振動プレス機(アサ
ヒエンジニアリング社製「振動プレス機SA−50」、
50トン)により、振動数750Hz、振幅10μmで
振動させて、表1に示す成形条件で深絞り成形品(厚さ
6mm×200×150×深さ100mm)を成形し
た。金型温度は上型125℃、下型140℃として6分
間成形した。尚、表1において、TaはSMCが上型及
び下型の両面に接してから、振動を開始するまで時間、
Tbは振動を停止するまでの時間をそれぞれ示す。ま
た、上記SMCのTk及びTpを前もって測定したとこ
ろ、それぞれ120秒及び180秒であり、これよりT
vを計算すると下記のようになる。 Tk+(Tp−Tk)/2=150≦Tv≦Tp+(Tp−Tk)=240
Using the above SMC, a vibration press machine (“vibration press machine SA-50” manufactured by Asahi Engineering Co., Ltd.,
50 tons), and a vibration was performed at a frequency of 750 Hz and an amplitude of 10 μm to form a deep-drawing molded product (thickness 6 mm × 200 × 150 × depth 100 mm) under the molding conditions shown in Table 1. Mold temperature was set to 125 ° C. for the upper mold and 140 ° C. for the lower mold for molding for 6 minutes. In Table 1, Ta is the time from when the SMC contacts both surfaces of the upper mold and the lower mold until the vibration starts,
Tb indicates the time until the vibration is stopped. Further, when the Tk and Tp of the SMC were measured in advance, they were 120 seconds and 180 seconds, respectively.
The calculation of v is as follows. Tk + (Tp−Tk) / 2 = 150 ≦ Tv ≦ Tp + (Tp−Tk) = 240

【0040】得られた成形品の立ち上がり面につき、表
面状態(くもりの有無等)を目視により評価すると共
に、光沢度として60度鏡面光沢度を測定し、その結果
を表1に示した。
The surface state (presence or absence of cloudiness, etc.) of the rising surface of the obtained molded product was visually evaluated, and a 60-degree specular gloss was measured as the gloss, and the results are shown in Table 1.

【0041】[0041]

【表1】 [Table 1]

【0042】[0042]

【発明の効果】本発明の深絞りプレス成形品の製造方法
の構成は、上述した通りであり、加熱プレス成形法にお
いて一定の時間金型を振動させることにより、立ち上が
り面の表面光沢や平滑性に優れた熱硬化性樹脂組成物の
深絞りプレス成形品を、大量に効率よく製造することが
できるので、FRP製の壁材、テーブルトップ、バスタ
ブ、洗面化粧台の製造に好適に用いられる。
The structure of the method for producing a deep-drawing press-formed product according to the present invention is as described above. By vibrating the die for a certain period of time in the hot press-forming method, the surface gloss and smoothness of the rising surface are increased. Since a deep-drawing press-formed product of the excellent thermosetting resin composition can be efficiently produced in a large amount, it is preferably used for producing FRP wall materials, table tops, bathtubs, and vanities.

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】熱硬化性樹脂組成物を上型と下型からなる
金型に供給して、深絞り形状を有する成形品を加熱プレ
ス成形する際に、加熱プレス工程で、下式で表されるT
vの時間範囲で金型を振動させることを特徴とする深絞
りプレス成形品の製造方法。 Tk+(Tp−Tk)/2≦Tv≦Tp+(Tp−Tk) (式中、Tkは、熱硬化性樹脂組成物が上型と下型の両
面に接触した時間を起点として、熱硬化性樹脂組成物が
急激に硬化発熱を開始するキックオフ点までの時間、T
pは最高発熱までの時間をそれぞれ示す)
1. When a thermosetting resin composition is supplied to a mold composed of an upper mold and a lower mold to hot press-mold a molded product having a deep drawing shape, the following formula is used in the hot pressing process. Done T
A method of manufacturing a deep-drawing press-formed product, which comprises vibrating a mold within a time range of v. Tk + (Tp−Tk) / 2 ≦ Tv ≦ Tp + (Tp−Tk) (In the formula, Tk is a thermosetting resin starting from the time when the thermosetting resin composition contacts both surfaces of the upper mold and the lower mold. The time to the kick-off point at which the composition suddenly begins to generate heat of curing, T
(p indicates the time to maximum fever, respectively)
JP9447193A 1993-04-21 1993-04-21 Production of deep draw press molded product Pending JPH06304942A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP9447193A JPH06304942A (en) 1993-04-21 1993-04-21 Production of deep draw press molded product

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP9447193A JPH06304942A (en) 1993-04-21 1993-04-21 Production of deep draw press molded product

Publications (1)

Publication Number Publication Date
JPH06304942A true JPH06304942A (en) 1994-11-01

Family

ID=14111202

Family Applications (1)

Application Number Title Priority Date Filing Date
JP9447193A Pending JPH06304942A (en) 1993-04-21 1993-04-21 Production of deep draw press molded product

Country Status (1)

Country Link
JP (1) JPH06304942A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB2401341A (en) * 2003-05-09 2004-11-10 Beldore Ltd A moulded former

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB2401341A (en) * 2003-05-09 2004-11-10 Beldore Ltd A moulded former
GB2401341B (en) * 2003-05-09 2006-08-16 Beldore Ltd Shower floor formers

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