JPS608034A - Extrusion molding of deformed and expanded product - Google Patents

Extrusion molding of deformed and expanded product

Info

Publication number
JPS608034A
JPS608034A JP58115089A JP11508983A JPS608034A JP S608034 A JPS608034 A JP S608034A JP 58115089 A JP58115089 A JP 58115089A JP 11508983 A JP11508983 A JP 11508983A JP S608034 A JPS608034 A JP S608034A
Authority
JP
Japan
Prior art keywords
die
sizer
extruded
molded
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.)
Pending
Application number
JP58115089A
Other languages
Japanese (ja)
Inventor
Tadaatsu Kasuga
春日 直温
Takeshi Banba
番場 武
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.)
Resonac Holdings Corp
Original Assignee
Showa Denko KK
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 Showa Denko KK filed Critical Showa Denko KK
Priority to JP58115089A priority Critical patent/JPS608034A/en
Publication of JPS608034A publication Critical patent/JPS608034A/en
Pending legal-status Critical Current

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C44/00Shaping by internal pressure generated in the material, e.g. swelling or foaming ; Producing porous or cellular expanded plastics articles
    • B29C44/34Auxiliary operations
    • B29C44/36Feeding the material to be shaped
    • B29C44/46Feeding the material to be shaped into an open space or onto moving surfaces, i.e. to make articles of indefinite length
    • B29C44/468Feeding the material to be shaped into an open space or onto moving surfaces, i.e. to make articles of indefinite length in a plurality of parallel streams which unite during the foaming
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C48/00Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
    • B29C48/25Component parts, details or accessories; Auxiliary operations
    • B29C48/88Thermal treatment of the stream of extruded material, e.g. cooling
    • B29C48/90Thermal treatment of the stream of extruded material, e.g. cooling with calibration or sizing, i.e. combined with fixing or setting of the final dimensions of the extruded article
    • B29C48/901Thermal treatment of the stream of extruded material, e.g. cooling with calibration or sizing, i.e. combined with fixing or setting of the final dimensions of the extruded article of hollow bodies
    • B29C48/903Thermal treatment of the stream of extruded material, e.g. cooling with calibration or sizing, i.e. combined with fixing or setting of the final dimensions of the extruded article of hollow bodies externally
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C48/00Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
    • B29C48/03Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor characterised by the shape of the extruded material at extrusion
    • B29C48/06Rod-shaped
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C48/00Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
    • B29C48/03Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor characterised by the shape of the extruded material at extrusion
    • B29C48/09Articles with cross-sections having partially or fully enclosed cavities, e.g. pipes or channels
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C48/00Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
    • B29C48/25Component parts, details or accessories; Auxiliary operations
    • B29C48/88Thermal treatment of the stream of extruded material, e.g. cooling
    • B29C48/885External treatment, e.g. by using air rings for cooling tubular films
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C48/00Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
    • B29C48/25Component parts, details or accessories; Auxiliary operations
    • B29C48/88Thermal treatment of the stream of extruded material, e.g. cooling
    • B29C48/911Cooling
    • B29C48/9115Cooling of hollow articles
    • B29C48/912Cooling of hollow articles of tubular films
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C48/00Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
    • B29C48/25Component parts, details or accessories; Auxiliary operations
    • B29C48/88Thermal treatment of the stream of extruded material, e.g. cooling
    • B29C48/919Thermal treatment of the stream of extruded material, e.g. cooling using a bath, e.g. extruding into an open bath to coagulate or cool the material

Landscapes

  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • Extrusion Moulding Of Plastics Or The Like (AREA)
  • Molding Of Porous Articles (AREA)

Abstract

PURPOSE:To mold deformed and expanded products having spiral projections with a great freedom of shape and dimension at low cost by a method in which an object to be extruded from the die having circularly arranged plural orifices is molded by rotation of a sizer. CONSTITUTION:The compound of a thermoplastic resin (e.g., polystyrene) and a blowing agent (e.g., azodicarbonamide) is charged into the hopper of an extruder 1 and extruded from a die 2 having circularly arranged plural orifices. The molten resin so extruded is molded by a sizer 5 and cooled in a cooling water tank 6, and an aimed product of an expansion ratio of 0.05-5, e.g., a cylinder or round bar whose periphery is provided with a spiral projection, is obtained by a takeout device 7. In the die 2, the land 8 of a comparatively large cross section is throttled into a small land 9 at the tip of the die, and the sizer 5 is turned through a chain 3 by a drive motor 4.

Description

【発明の詳細な説明】 本発明は円筒又は丸棒の外周に螺旋状の突起部を有する
発泡倍率005〜5倍の発泡異形押出成形品の成形法に
関する。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for forming a foamed profile extrusion molded product having a spiral protrusion on the outer periphery of a cylinder or round bar and having an expansion ratio of 005 to 5 times.

本発明の目的は、断面が円形の丸棒又は円筒の外周に螺
旋状の突起部を有する種々の発泡異形押出成形品を得る
ことにあシ、との成形品の具体的な用途としては、家具
類の部品、粉体輸送用スクリュー、掃除機吸込口の回転
ブラシ台、ケーブル類の支持体、液体輸送時のスタティ
ックミキサー、光ファ°イバーのスペーサー等が上げら
れる。
The purpose of the present invention is to obtain various foamed profile extrusion molded products having a spiral protrusion on the outer periphery of a round bar or cylinder having a circular cross section.Specific uses of the molded product include: Examples include furniture parts, screws for transporting powder, rotating brush stands for vacuum cleaner suction ports, supports for cables, static mixers for transporting liquids, spacers for optical fibers, etc.

以下に本発明の概要を図面によって説明すると、第1図
の側面図において、熱可ソ性樹脂と発泡剤を混合したコ
ンパウンドを押出機1のホッパーより投入してダイス2
より押出す。押出された溶融樹脂はサイザー5によって
賦形され、次いで冷却水槽6によって冷却され、引取機
7によって引取られる。
The outline of the present invention will be explained below with reference to the drawings. In the side view of FIG.
Push out more. The extruded molten resin is shaped by a sizer 5, then cooled by a cooling water tank 6, and taken by a take-off machine 7.

ダイス2は第2図の断面図(左側)及び正面図(右側)
に示すような構造をしており、比較的断面積の大きなラ
ンド8からダイス先端において細でいる。サイザー5は
チェーン3を通じて駆動モレン、ポリプロピレン、ポリ
スチレン、ポリ塩化ビニル、ABS、As、ポリカーボ
ネート、ナイロン等押出機により連続的に押出可能な樹
脂が上げられ、発泡させるには、固体発泡剤、気体発泡
剤のいずれも採用でき、発泡倍率lio、05〜5倍好
ましくは0.1〜3倍であり、005倍未満では賦形が
困難であり、5倍を越えると成形品の強度が低下して実
用上問題となる。々おここにおける発泡倍率は無発泡状
態の密度を発泡後の密度で除した商(倍)から1(倍)
を差引いたものである。
Dice 2 is the cross-sectional view (left side) and front view (right side) of Figure 2.
It has a structure as shown in FIG. 1, with a land 8 having a relatively large cross-sectional area and a narrow end at the tip of the die. The sizer 5 is driven by a chain 3, and resins such as molene, polypropylene, polystyrene, polyvinyl chloride, ABS, As, polycarbonate, and nylon that can be continuously extruded by an extruder are raised through the drive chain 3. Any foaming agent can be used, and the expansion ratio lio is 0.5 to 5 times, preferably 0.1 to 3 times. If it is less than 0.05 times, shaping is difficult, and if it exceeds 5 times, the strength of the molded product will decrease. This poses a practical problem. The foaming ratio here is 1 (times) from the quotient (times) of the unfoamed density divided by the density after foaming.
is obtained by subtracting .

サイザーを回転させることによる。螺旋部のピッチはサ
イザーの回転数および引取速度によって決まる。
By rotating the sizer. The pitch of the helix is determined by the sizer's rotational speed and take-up speed.

以下本発明の効果について述べる。The effects of the present invention will be described below.

丸棒又は円筒の外周に螺旋状突起部のついた異この方法
では複雑々分割金型を使用しなければならず全型代が高
価につくし、金型分割部の線が成形品に現われて外観上
好ましくない。又、射出成形では発泡倍率を高めること
が困難である。又、成形品の断面積が大きくなると冷却
に時間がかかる為成形サイクルが長くなり、成形コスト
が高くつく。更に、成形品の長さが1mを越えるような
長尺品を成形する場合、射出成形では無理がある。
This method uses a round bar or cylinder with a spiral protrusion on its outer periphery. This method requires the use of complexly divided molds, which increases the total mold cost, and the lines of the mold divisions may appear on the molded product. Unfavorable in appearance. Furthermore, in injection molding, it is difficult to increase the expansion ratio. Furthermore, as the cross-sectional area of the molded product becomes larger, it takes longer to cool down, resulting in a longer molding cycle and higher molding costs. Furthermore, when molding a long product with a length exceeding 1 m, injection molding is difficult.

押出成形によって螺旋状突起部のついた成形品をつくる
場合、ダイス、サイザーは固定とし、成形品を回転させ
ながら引取る方法も可能であるが、引取機の機構が複雑
になり、高価になる。又、回転と引取を独立に作動させ
る様な機構を備えた引取機をつくることは更に高価に々
る可能性がある。
When making a molded product with a spiral protrusion by extrusion molding, it is possible to fix the die and sizer and take the molded product while rotating, but the mechanism of the take-off machine becomes complicated and expensive. . Furthermore, it may be even more expensive to create a take-up machine equipped with a mechanism that independently operates rotation and take-up.

それに対して本発明のようにサイザーを回転させ、引取
機は通常のものを使用する方が成形品形状に対する自由
度が大きいし、機械の製作価格も安価である。
On the other hand, if the sizer is rotated and a normal take-off machine is used as in the present invention, the degree of freedom regarding the shape of the molded product is greater, and the manufacturing cost of the machine is also lower.

本発明では螺旋状突起部を有する異形成形品は同時に発
泡成形品であるが、第2図に示す様な構造を有するダイ
スと回転サイザーの組合せによりはじめて良好な発泡異
形成形品が得られる。円筒の外周に突起部を有する成形
品をつくりたい場合は、第2図においてダイスの中心の
孔10より空気を吹込むか、サイザーを真空にひいて成
形することができる。
In the present invention, the irregularly shaped article having a spiral protrusion is also a foamed article, but a good foamed irregularly shaped article can only be obtained by combining a die having a structure as shown in FIG. 2 and a rotary sizer. If it is desired to make a molded product having a protrusion on the outer periphery of a cylinder, the molding can be performed by blowing air through the hole 10 in the center of the die, as shown in FIG. 2, or by evacuating the sizer.

良好な発泡成形品を得るには溶融した蓄槽#カ樹脂がダ
イスから押出された時点で過発泡の状態になら々い様制
御しなくてはならないが、第2図の断面図に示した様な
構造のダイスを用いるとダイスのランド方向における圧
力勾配が大きく、ダイス内における発泡現象による肌ア
レ状態を防止できる。ダイス構造が不適当々場合はダイ
ス内で発泡剤が分解し、ひどい肌アレ状態で樹脂が押出
されてくるので良好な成形品が得られない。
In order to obtain a good foamed molded product, it is necessary to control the molten resin from the storage tank so that it does not become over-foamed when it is extruded from the die. When a die with a similar structure is used, the pressure gradient in the land direction of the die is large, and it is possible to prevent skin irritation due to foaming inside the die. If the die structure is inappropriate, the blowing agent will decompose within the die and the resin will be extruded with severe skin irritation, making it impossible to obtain a good molded product.

ダイスから出てきた溶融樹脂は当初何本かのストランド
状に押出されるが、発泡作用により膨張する為、ストラ
ンド同志が接着し、更にサイザーによって外部からおさ
えられる為内部に向って発泡作用を続は一本の棒状体を
形成する。又、螺旋状突起部の断面形状は四角形、三角
形、半円形等、巾、高さを含めて適宜採用できる。突起
部の条数も要求される形状に合せて適宜採用できる。
The molten resin that comes out of the die is initially extruded into several strands, but as it expands due to the foaming action, the strands adhere to each other, and are further suppressed from the outside by the sizer, so the foaming action continues inward. forms a rod. Further, the cross-sectional shape of the spiral protrusion may be square, triangular, semicircular, etc., including the width and height, as appropriate. The number of protrusions can also be appropriately selected depending on the required shape.

以上のように本発明によれば、螺旋状突起部を有する発
泡異形成形品を形状、寸法の大きな自由度をもって、安
価に成形できる。
As described above, according to the present invention, a foamed irregularly shaped article having a spiral protrusion can be formed at low cost with a large degree of freedom in shape and size.

以下、実施例を示して本発明をさらに詳細に説明する。Hereinafter, the present invention will be explained in more detail by showing examples.

実施例 メルトフローレート49 / mjnのポリスチレン1
00重量部に発泡剤ADOA(アゾジカルボンアミド)
1.0重量部、発泡助剤タルク0.15重量部をトライ
ブレンドし、バレル径65mmの単軸押出機を用い、直
径35mmの円周上に等間隔に中心を置く8個の内径2
mmの円孔状オリフィスから第2図に示すようダイスよ
り押出速度100 mm/mm 。
Example polystyrene with melt flow rate 49/mjn 1
00 parts by weight of blowing agent ADOA (azodicarbonamide)
1.0 parts by weight of foaming aid talc and 0.15 parts by weight of talc were triblended, and using a single-screw extruder with a barrel diameter of 65 mm, 8 inner diameter 2 pieces centered at equal intervals on a circumference of 35 mm diameter were triblended.
The extrusion speed was 100 mm/mm from the die as shown in FIG.

引取速度250mm1mmで溶融押出した後、回転サイ
ザーにより賦形した。
After melt-extruding at a take-up speed of 250 mm and 1 mm, it was shaped using a rotary sizer.

なお前記円周中心に位置する直径6mmの孔から加圧空
気を吹込み、回転サイザーの内部は長さ300mm、テ
ーパーなしで胴径40mmであり、径8mmの断面半円
径の凹溝を8本等間隔に有し、毎分1/2回転である。
Pressurized air was blown through a hole with a diameter of 6 mm located at the center of the circumference, and the inside of the rotary sizer had a length of 300 mm, a body diameter of 40 mm without a taper, and a concave groove with a semicircular cross section of 8 mm in diameter. The rotation speed is 1/2 rotation per minute.

得られた成形品は胴径40mmで8条の断面半円形で底
辺8mm、高さ4mmの突条部の輪郭を有し、ピッチ5
001mの螺旋状の突起部を有する外観良好な発泡倍率
25倍の発泡異形押出成形品であった。
The obtained molded product had a body diameter of 40 mm, a semicircular cross section of 8 strips, a protrusion profile with a base of 8 mm, a height of 4 mm, and a pitch of 5.
It was a foamed profile extrusion molded product having a spiral protrusion of 0.001 m and a good appearance and a foaming ratio of 25 times.

【図面の簡単な説明】[Brief explanation of the drawing]

第1図は本発明の概要を示す側面図、第2図は同じく断
面図(左側)及び正面図(右側)である。 1・押出機、2 ダイス、3・・・チェーン、4駆動モ
ーター、5 サイザー、6 冷却水槽、7・・引取機、
8 比較的断面積の大きなランド、9 細いランド、]
0・・・孔 特許出願人 昭和電工株式会社 代理 人弁理士 菊地精− 第1図 第2図
FIG. 1 is a side view showing an outline of the present invention, and FIG. 2 is a sectional view (left side) and a front view (right side). 1. Extruder, 2. Dice, 3.. Chain, 4. Drive motor, 5. Sizer, 6. Cooling water tank, 7.. Taking machine.
8 Land with relatively large cross-sectional area, 9 Thin land, ]
0...Ko Patent applicant Showa Denko K.K. Patent attorney Sei Kikuchi - Figure 1 Figure 2

Claims (1)

【特許請求の範囲】[Claims] 円筒又は丸棒の外周に螺旋状の突起部を有する発泡倍率
0.05〜5倍の発泡異形押出成形品を成形する際、複
数−のオリフィスを円形に配置したダイスからの押出物
をサイザーの回転により賦形することを特徴とする発泡
異形押出成形法。
When molding a foamed profile extrusion molded product with a foaming ratio of 0.05 to 5 times, which has a spiral protrusion on the outer periphery of a cylinder or round bar, the extrudate from a die with a plurality of orifices arranged in a circular manner is passed through a sizer. A foaming profile extrusion molding method characterized by shaping by rotation.
JP58115089A 1983-06-28 1983-06-28 Extrusion molding of deformed and expanded product Pending JPS608034A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP58115089A JPS608034A (en) 1983-06-28 1983-06-28 Extrusion molding of deformed and expanded product

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP58115089A JPS608034A (en) 1983-06-28 1983-06-28 Extrusion molding of deformed and expanded product

Publications (1)

Publication Number Publication Date
JPS608034A true JPS608034A (en) 1985-01-16

Family

ID=14653920

Family Applications (1)

Application Number Title Priority Date Filing Date
JP58115089A Pending JPS608034A (en) 1983-06-28 1983-06-28 Extrusion molding of deformed and expanded product

Country Status (1)

Country Link
JP (1) JPS608034A (en)

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