JPS6283109A - Resin supplyer for molding machine - Google Patents

Resin supplyer for molding machine

Info

Publication number
JPS6283109A
JPS6283109A JP60225505A JP22550585A JPS6283109A JP S6283109 A JPS6283109 A JP S6283109A JP 60225505 A JP60225505 A JP 60225505A JP 22550585 A JP22550585 A JP 22550585A JP S6283109 A JPS6283109 A JP S6283109A
Authority
JP
Japan
Prior art keywords
resin
molding machine
hopper
gas
screw
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.)
Granted
Application number
JP60225505A
Other languages
Japanese (ja)
Other versions
JPH0684013B2 (en
Inventor
Tatsumi Takahashi
達見 高橋
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.)
Dai Nippon Printing Co Ltd
Original Assignee
Dai Nippon Printing 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 Dai Nippon Printing Co Ltd filed Critical Dai Nippon Printing Co Ltd
Priority to JP60225505A priority Critical patent/JPH0684013B2/en
Publication of JPS6283109A publication Critical patent/JPS6283109A/en
Publication of JPH0684013B2 publication Critical patent/JPH0684013B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime 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
    • B29C45/00Injection moulding, i.e. forcing the required volume of moulding material through a nozzle into a closed mould; Apparatus therefor
    • B29C45/17Component parts, details or accessories; Auxiliary operations
    • B29C45/18Feeding the material into the injection moulding apparatus, i.e. feeding the non-plastified material into the injection unit
    • 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
    • B29C48/285Feeding the extrusion material to the extruder
    • B29C48/29Feeding the extrusion material to the extruder in liquid form
    • 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
    • B29C48/285Feeding the extrusion material to the extruder
    • B29C48/295Feeding the extrusion material to the extruder in gaseous form
    • 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

Landscapes

  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • Manufacturing & Machinery (AREA)
  • Processing And Handling Of Plastics And Other Materials For Molding In General (AREA)
  • Injection Moulding Of Plastics Or The Like (AREA)
  • Extrusion Moulding Of Plastics Or The Like (AREA)

Abstract

PURPOSE:To permit powdery resin to be dropped stably by using a system in which a gas is blown into a supplying section for the powdery resin between a hopper and then molding machine body. CONSTITUTION:A supporter 2 is attached to the lower end of a hopper for powdery resin as a raw material, and a supply port 6 with fitting seat plate 5 is provided to the cylinder 4 of a screw 3. A ring like spacer 8 with a pipe 7 through which a gas is blown out is provided between the supply port 6 and the seat plate 5 of the cylinder 4. The pipe 7 is bent to be directed toward the hopper. The spacer 8 can be attached by vertically moving the hopper 1.

Description

【発明の詳細な説明】 (産業上の利用分野) 本発明は、射出成形機、押出機(ラム押出機)(以下、
成形機という)等の成形機の分野に属し、詳しくはホッ
パより成形機に原料の樹脂を安定して供給するための樹
脂供給装置に関するものである。
Detailed Description of the Invention (Industrial Application Field) The present invention relates to an injection molding machine, an extruder (ram extruder) (hereinafter referred to as
It belongs to the field of molding machines such as molding machines, etc., and specifically relates to a resin supply device for stably supplying raw material resin from a hopper to a molding machine.

(従来の技術) 樹脂の成形を安定させるための要因としては、スクリュ
ーの形状、その回転数、シリンダ又はバレルの温度、金
型の形状、その温度、ダイスの形状、その温度等が挙げ
られる。しかしながら、これらの要因は、すでに供給さ
れた樹脂が溶融して、ある程度の流動性を帯びた状態で
の制御であり、樹脂が熔融する前に、不安定な原料樹脂
の供給がされていたならば、安定した成形を行うことは
困難になる場合が多くなる。
(Prior Art) Factors for stabilizing resin molding include the shape of the screw, its rotation speed, the temperature of the cylinder or barrel, the shape of the mold, its temperature, the shape of the die, its temperature, etc. However, these factors are controlled when the supplied resin has already melted and has a certain degree of fluidity, and if unstable raw material resin had been supplied before the resin melted, In many cases, it becomes difficult to perform stable molding.

そして、この原料の樹脂も、その状態、すなわちペレッ
ト状あるいは粉体状のものによっても異なるものである
The raw material resin also differs depending on its state, ie, whether it is in the form of pellets or powder.

一般に樹脂は、原料の製造時には、粉体状のものが多い
が、粉体状であると運搬時に破袋した場合や、成形機に
供給する場合等に周囲に飛散することがある。これがた
め、高分子材料の樹脂はペレタイズされて、ある程度の
大きさに切断されたベレットの状態で供給されている。
Generally, resin is often in powder form when producing raw materials, but if it is in powder form, it may be scattered around when the bag is broken during transportation or when it is supplied to a molding machine. For this reason, the polymeric resin is supplied in the form of pellets that are pelletized and cut into a certain size.

ところが、高分子材料の中には、ペレタイズができずに
粉体状のまま供給されるものもある。
However, some polymeric materials cannot be pelletized and are supplied in powder form.

例えば、塩化ビニール、フロロカーボン、超高分子量ポ
リエチレン等である。
For example, vinyl chloride, fluorocarbon, ultra-high molecular weight polyethylene, etc.

成形にあたって、樹脂の形態がベレット状がよいか、粉
体状がよいかは、樹脂の種類と成形機のスクリューの径
によって決まる。
When molding, whether the resin should be in pellet form or powder form is determined by the type of resin and the diameter of the molding machine's screw.

スクリューの径が40B以上の場合は、樹脂の形態に依
存しない場合が多く、スクリューの径が40m+w以下
の場合は、樹脂の形態に依存することが多い。
When the diameter of the screw is 40B or more, it often does not depend on the form of the resin, and when the diameter of the screw is 40m+w or less, it often depends on the form of the resin.

特にスクリューの径が18w以下になると、スクリュー
の強度上の問題から、フライトの高さに限界があり、ベ
レットの寸法よりフライトが小さくなる場合がある。こ
の場合は、スクリューの供給部で、樹脂が供給されない
という問題が発生する。この場合の解決手段の一つは、
樹脂の形態を粉体状にすることにより解決することがで
きるが、粉体状にすると供給自体が不安定になる場合が
多くなる。
In particular, when the diameter of the screw is 18W or less, there is a limit to the height of the flight due to problems with the strength of the screw, and the flight may become smaller than the dimensions of the pellet. In this case, a problem arises in that the resin is not supplied at the supply section of the screw. One solution in this case is
This problem can be solved by changing the form of the resin to a powder, but if the resin is made into a powder, the supply itself becomes unstable in many cases.

そこで、粉体状の樹脂を安定的にスクリ1−の供給部へ
供給する方法としては、供給部の上部に強制的な供給の
ためのスクリューを設ける方法、あるいは供給部の粉体
状の樹脂に、機械的振動、又は超音波的振動を加える等
があり、これにより粉体状の樹脂の落下を促進させ、ま
た滞留を防いでいる。
Therefore, as a method for stably supplying powdered resin to the supply section of the screw 1-, there is a method of providing a screw for forced feeding at the top of the supply section, or a method of supplying powdered resin in the supply section. In addition, mechanical vibration or ultrasonic vibration is applied, which promotes the falling of the powdered resin and prevents it from stagnation.

(発明が解決しようとする問題点) 上記の第1の2方法の問題点は、供給用のスクリューの
形状、寸法が、使用するホッパの寸法形状や、使用す゛
る成形機の機能に応じて別個に設計しなければならず、
かつこのスクリューを回転する動力源の設置まで考慮す
る必要から高価なものとなることがある。
(Problems to be Solved by the Invention) The problem with the first two methods above is that the shape and dimensions of the feeding screw vary depending on the dimensions and shape of the hopper used and the functions of the molding machine used. must be designed to
In addition, it is necessary to consider the installation of a power source for rotating this screw, which may result in an expensive product.

第2の方法の問題点は、第1の方法と同様に機械的振動
を加える場合には、外部からの動力源が必要となり、小
形の成形機に設置するには困難であり、また超音波振動
を加える場合には、固有振動数を見い出さなくてはなら
ず、面倒な問題を生ずる。
The problem with the second method is that when applying mechanical vibration like the first method, an external power source is required, which is difficult to install in a small molding machine, and ultrasonic When applying vibration, the natural frequency must be found, which creates a complicated problem.

(問題点を解決するための手段) 本発明考は、以上の問題点を解決すべく種々研究を重ね
た結果、粉体状の樹脂が成形機のスクリューの供給部に
安定的に自然落下しないのは、粉体になるとベレットの
場合と異なり、樹脂の表面積が増大するとともに、粉体
の複雑な形状が個々にからみあって、自然落下が不安定
になることから、この粉体粒子の個々に外部より気体を
供給すれば、粒子間の間隔をあけられることができ、粒
子間の摩擦がなくなって安定した自然落下ができること
を発見した。
(Means for Solving the Problems) The idea of the present invention is that, as a result of various studies to solve the above problems, powdered resin does not fall down by itself in a stable manner into the feeding section of the screw of the molding machine. This is because, unlike in the case of pellets, when powdered, the surface area of the resin increases, and the complex shapes of the powder become intertwined with each other, making their natural fall unstable. They discovered that by supplying gas from the outside, the particles can be spaced apart, eliminating friction between particles and allowing stable natural fall.

そして、本発明はこれに基づいてなされたもので、ホッ
パと成形機本体との間の粉体状の樹脂の供給部に気体を
吹き込むようにしたものである。
The present invention has been made based on this, in which gas is blown into a powder resin supply section between the hopper and the molding machine body.

(実施例) 以下、本発明の実施例を図面に基づいて説明する。(Example) Embodiments of the present invention will be described below based on the drawings.

図面は、本発明の装置を示す断面図である。The drawing is a cross-sectional view of the device of the invention.

原料の粉体状の樹脂ホッパ(1)の下端には支持部材(
2)が取付けられており、スクリュー(3)のシリンダ
(4)には取付座板(5)付の供給口(6)が設けられ
ている。
The support member (
2) is attached, and the cylinder (4) of the screw (3) is provided with a supply port (6) with a mounting seat plate (5).

このホッパ(1)の支持部材(2)と、シリンダ(4)
の供給口(6)の取付座板(5)との間には、本発明の
重要な構成をなす気体吹出用のパイプ(7)付のリング
状スペーサー(8)が介装されている。このパイプ(7
)は、ホッパ(1)の方向に向かうように屈曲している
The support member (2) of this hopper (1) and the cylinder (4)
A ring-shaped spacer (8) with a gas blowing pipe (7), which is an important component of the present invention, is interposed between the supply port (6) and the mounting seat plate (5). This pipe (7
) is bent toward the hopper (1).

スペーサー(8)は、ホッパ(1)を上下方向に動かず
ことによって装着することができるものである。
The spacer (8) can be installed without moving the hopper (1) in the vertical direction.

リング状スペーサー (8)の厚さをD、その内径をA
゛、スペーサー(8)の中の上方に向かうパイプの高さ
をh、その内径をd、シリンダ(4)の供給口(6)の
内径をAとすると、成形機の規模により差は出てくるが
、好ましい関係は次のようになる。
The thickness of the ring-shaped spacer (8) is D, and its inner diameter is A.
゛, Assuming that the height of the upward pipe inside the spacer (8) is h, its inner diameter is d, and the inner diameter of the supply port (6) of the cylinder (4) is A, there will be differences depending on the scale of the molding machine. However, the preferred relationship is as follows.

A’  ≦A      ・ ・ ・ ・ ・■D  
≦A″     ・ ・ ・ ・ ・■1/3 D≦h
≦3D  ・ ・ ・■1/100 A’≦d<A’ 
 ・・■ここで、成形機の樹脂供給口が長方形の場合は
、Aは対角線の長さである。
A' ≦A ・ ・ ・ ・ ・■D
≦A″ ・ ・ ・ ・ ・■1/3 D≦h
≦3D ・ ・ ・■1/100 A'≦d<A'
...■Here, if the resin supply port of the molding machine is rectangular, A is the length of the diagonal.

パイプ(7)より送る気体の量は、必要とする気体の圧
力で表現することにすると、I KPa〜15MPaで
あり、好ましくは10KPa〜10MPaである。
The amount of gas sent from the pipe (7), expressed in terms of the required gas pressure, is I KPa to 15 MPa, preferably 10 KPa to 10 MPa.

使用する気体の種類は、乾燥空気、窒素ガス、フレオン
ガス、ヘリウムガス等の不活性気体が好ましい。
The type of gas used is preferably an inert gas such as dry air, nitrogen gas, Freon gas, or helium gas.

なお、気体の吹出し用パイプの数は1本でも複数本であ
ってもよいが、断面積合計が上記の■の条件を満足する
ことが必要である。
The number of gas blowing pipes may be one or more, but it is necessary that the total cross-sectional area satisfies the condition (2) above.

また、使用する気体の供給方式は、連続的にホッパ内に
供給するか、間歇的に供給してもよい。間歇的に供給す
る場合の周期は 10 sec〜10 secであり、好ましくは10 
sec〜10secである。
Further, the gas used may be supplied continuously into the hopper or intermittently. The cycle in the case of intermittent supply is 10 sec to 10 sec, preferably 10 sec.
sec to 10 sec.

次に、具体的な寸法が、A =5011rm、 D =
40+*、h =6(hm、 d =1.0 mの気体
供給装置を造り、これを型締力が22ton 、スクリ
ューの径が18mの射出成形機に装着して、窒素ガスを
0.5Paの圧力で使用した。
Next, the specific dimensions are A = 5011rm, D =
40+*, h = 6 (hm, d = 1.0 m), and installed this in an injection molding machine with a mold clamping force of 22 tons and a screw diameter of 18 m, and supplied nitrogen gas at 0.5 Pa. It was used at a pressure of

使用した樹脂は、超高分子量ポリエチレン(三井石油化
学工業製のハイゼソクスミリオン240M)であり、射
出成形の条件は、スクリューによる可塑化時間を7秒、
射出時間を2秒、キユアリング時間を10秒、取出し時
間を1.5秒、インターバルを4秒、全体のサイクル時
間を23秒とした。
The resin used was ultra-high molecular weight polyethylene (Hize Sox Million 240M manufactured by Mitsui Petrochemical Industries), and the injection molding conditions were: plasticization time with a screw of 7 seconds;
The injection time was 2 seconds, the curing time was 10 seconds, the ejection time was 1.5 seconds, the interval was 4 seconds, and the total cycle time was 23 seconds.

これによる成形品の形状は、直径60m、厚さ3nの円
板状の中心部に直径1511、高さ61mの凸部があり
、その中央部にゲートを設けたものである。
The shape of the resulting molded product was a disc-shaped center with a diameter of 60 m and a thickness of 3 nm, with a convex part having a diameter of 1511 m and a height of 61 m at the center, and a gate was provided in the central part.

この成形品を、本発明におけるスペーサーを使用しない
で射出成形した場合は、1000シヨツトしたもののう
ちからランダムに50個を抽出して、そのM量を測定し
たところ、そのばらつきは0.56%であった。これに
対して、本発明の装置により射出成形した場合は、10
00シヨツトしたもののうちからランダムに50個を抽
出して測定した結果は、0.05%のばらつきであって
、スペーサーを使用しないものの約1/10である。
When this molded product was injection molded without using the spacer of the present invention, 50 pieces were randomly selected from 1000 shots and the amount of M was measured, and the variation was 0.56%. there were. On the other hand, when injection molding is performed using the apparatus of the present invention, 10
The results of measuring 50 samples randomly selected from 0.00 shots had a variation of 0.05%, which was about 1/10 of that obtained without using a spacer.

(発明の効果) 本発明は、樹脂ホッパと成形機本体との間の樹脂供給部
に気体の吹出口を設けただけのものであるにもかかわら
ず、例えば超高分子量ポリエチレン等の粉体状の樹脂を
供給する場合に、成形機本体への安定した供給ができ、
これによって精度が高く品質のよい成形品を効率よく生
産することができる。
(Effects of the Invention) Although the present invention only provides a gas outlet in the resin supply section between the resin hopper and the molding machine body, it is possible to When supplying resin to the molding machine body, stable supply is possible.
This makes it possible to efficiently produce molded products with high precision and good quality.

しかも、どの成形機にも設置することができて、安定的
に作動し、故障が少なく、安価に提供することができる
Moreover, it can be installed in any molding machine, operates stably, has few failures, and can be provided at low cost.

なお、気体吹出口からの不活性気体は、シリンダ内の樹
脂の酸化を防ぎ、分子量の低下を防ぐ作用をもするもの
である。
Note that the inert gas from the gas outlet also functions to prevent oxidation of the resin within the cylinder and prevent a decrease in molecular weight.

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

図面は本発明の装置の断面図である。 符号1・・・・ホッパ 2・・・・支持部材 3・・・・スクリュー 4・・・・シリンダ 5・・・・取付座板 6・・・・供給口 ア・・・・パイプ 8・・・・リング状スペーサー The drawing is a cross-sectional view of the device of the invention. Code 1...Hopper 2...Supporting member 3...Screw 4...Cylinder 5...Mounting seat plate 6... Supply port A...pipe 8...Ring-shaped spacer

Claims (4)

【特許請求の範囲】[Claims] (1)ホッパよりの成形機本体への樹脂供給部に気体吹
出口を設けた成形機における樹脂供給装置。
(1) A resin supply device for a molding machine in which a gas outlet is provided in the resin supply section from the hopper to the molding machine main body.
(2)気体吹出口の向きがホッパ方向である特許請求の
範囲第1項記載の成形機における樹脂供給装置。
(2) The resin supply device for a molding machine according to claim 1, wherein the gas outlet is oriented toward the hopper.
(3)気体吹出口の数が単数又は複数である特許請求の
範囲第1項及び第2項記載の成形機における樹脂供給装
置。
(3) The resin supply device for a molding machine according to claims 1 and 2, wherein the number of gas blow-off ports is single or plural.
(4)気体吹出口よりの気体の吹出しが連続的又は間歇
的である特許請求の範囲第1項乃至第3項記載の成形機
における樹脂供給装置。
(4) A resin supply device for a molding machine according to any one of claims 1 to 3, wherein the gas is continuously or intermittently blown out from the gas outlet.
JP60225505A 1985-10-09 1985-10-09 Resin supply device in molding machine Expired - Lifetime JPH0684013B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP60225505A JPH0684013B2 (en) 1985-10-09 1985-10-09 Resin supply device in molding machine

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP60225505A JPH0684013B2 (en) 1985-10-09 1985-10-09 Resin supply device in molding machine

Publications (2)

Publication Number Publication Date
JPS6283109A true JPS6283109A (en) 1987-04-16
JPH0684013B2 JPH0684013B2 (en) 1994-10-26

Family

ID=16830369

Family Applications (1)

Application Number Title Priority Date Filing Date
JP60225505A Expired - Lifetime JPH0684013B2 (en) 1985-10-09 1985-10-09 Resin supply device in molding machine

Country Status (1)

Country Link
JP (1) JPH0684013B2 (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2007276403A (en) * 2006-04-11 2007-10-25 Asmo Co Ltd Molding device and molding method
JP2014074094A (en) * 2012-10-03 2014-04-24 Mitsubishi Engineering Plastics Corp Method for producing flame-retardant thermoplastic resin composition

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5148662A (en) * 1974-08-28 1976-04-26 Hoffmann La Roche

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5148662A (en) * 1974-08-28 1976-04-26 Hoffmann La Roche

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2007276403A (en) * 2006-04-11 2007-10-25 Asmo Co Ltd Molding device and molding method
JP2014074094A (en) * 2012-10-03 2014-04-24 Mitsubishi Engineering Plastics Corp Method for producing flame-retardant thermoplastic resin composition

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