JPS5913336B2 - Screw for extruder - Google Patents

Screw for extruder

Info

Publication number
JPS5913336B2
JPS5913336B2 JP51028651A JP2865176A JPS5913336B2 JP S5913336 B2 JPS5913336 B2 JP S5913336B2 JP 51028651 A JP51028651 A JP 51028651A JP 2865176 A JP2865176 A JP 2865176A JP S5913336 B2 JPS5913336 B2 JP S5913336B2
Authority
JP
Japan
Prior art keywords
screw
section
resin
extruder
flight
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
JP51028651A
Other languages
Japanese (ja)
Other versions
JPS52112655A (en
Inventor
隆 島野
勝己 折茂
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.)
Furukawa Electric Co Ltd
Original Assignee
Furukawa Electric 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 Furukawa Electric Co Ltd filed Critical Furukawa Electric Co Ltd
Priority to JP51028651A priority Critical patent/JPS5913336B2/en
Publication of JPS52112655A publication Critical patent/JPS52112655A/en
Publication of JPS5913336B2 publication Critical patent/JPS5913336B2/en
Expired 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
    • 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
    • B29C48/36Means for plasticising or homogenising the moulding material or forcing it through the nozzle or die
    • B29C48/50Details of extruders
    • B29C48/505Screws
    • B29C48/55Screws having reverse-feeding elements
    • 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
    • B29C48/36Means for plasticising or homogenising the moulding material or forcing it through the nozzle or die
    • B29C48/50Details of extruders
    • B29C48/505Screws
    • B29C48/53Screws having a varying channel depth, e.g. varying the diameter of the longitudinal screw trunk

Description

【発明の詳細な説明】 本発明は熱可塑性樹脂を可塑化して押出す押出機に用い
るスクリューの改良に関するものである。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to an improvement in a screw used in an extruder for plasticizing and extruding a thermoplastic resin.

従来熱可塑性樹脂の押出に使用されている押出機はバレ
ル内にスクリューを設け、これを回転させることにより
熱可塑性樹脂を可塑化し、バ5 レルの先端に設けたダ
イより押出し形成する形式のものでバレル内の熱可塑性
樹脂を可塑化する部分は第3図に示すようにスクリュー
の芯体1’に樹脂送り用フライト2’を設け、このフラ
イトzで構成されるスクリューのらせん0 溝3を軸線
方向へ順番に最初は、すなわち供給部では比較的深くし
てホッパー(図示していない)から供給される熱可塑性
樹脂を移送し、次に、すなわち圧縮部ではらせん溝gを
押出方向に順次浅くして、ここで樹脂を加熱混練すると
ともに樹脂5 の押出圧力を高め、最後に、すなわち計
量部ではらせん溝3を一様な浅い溝とし、この狭い流通
路に沿うて樹脂が流れることにより樹脂が均一に混練溶
融されるとともに樹脂圧力を所望圧に保持しこれにより
計量して、先端に設けたダイ(図示し’0 てない)よ
り押出すものである。従つてこのような形式の押出機の
押出量はらせん溝3の浅い部分で決まわ、この部分の溝
の深さを深くすれば同サイズのスクリューでも押出量を
増加できるはずであるが、そうすると次のような問題が
生じる。即フ5 ち樹脂のかさ比重は固状の状態と溶融
状態とで違つておわ、後者の分が大きいので、スクリュ
ー先端部の溝の深さを深くするとスクリュー先端部から
樹脂が早く押出され、スクリューの中間部に樹脂のつま
つていない部分が生じ、押出が不安定にノ0 なるので
ある。またこのような浅い溝部分のあるスクリューによ
り多量の樹脂を押出そうとすると、樹脂のせん断による
摩擦熱が多量に発生し、樹脂温度のコントロールが困難
になる。これがため押出量を増大するには押出機を大型
のものにするか、?5 強制冷却装置を付加するかして
いるが、設備コストがかさみ、特に後者の場合には樹脂
の熱伝導率が小さいため局部的な加熱が生じ、押出性能
に悪影響があつた。本発明はこれに鑑み、本発明によれ
ば、熱可塑性樹脂を供給される供給部とこの供給部から
の移送されてくる樹脂の圧力を高める圧縮部と樹脂の押
出量を計量する計量部とを軸線方向へ順番に有し押出機
のバL/ル内に設置されるスクリユ一において、計量部
に}ける樹脂送ジ用フライトの向きを供給部卦よび圧縮
部における樹脂送り用フライトの向きとは逆にし、スク
リユ一の芯体を供給部、圧縮部、および計量部において
一様な太さとする。
The extruder conventionally used to extrude thermoplastic resin has a screw installed in the barrel, which rotates to plasticize the thermoplastic resin, which is then extruded through a die installed at the tip of the barrel. As shown in Fig. 3, the part where the thermoplastic resin inside the barrel is plasticized is provided with a flight 2' for resin feeding on the core body 1' of the screw, and a helix 0 groove 3 of the screw consisting of this flight z. The thermoplastic resin fed from a hopper (not shown) is transferred in the axial direction first, i.e. in a relatively deep manner in the feeding section, and then in the compression section in the helical groove g sequentially in the extrusion direction. Here, the resin is heated and kneaded and the extrusion pressure of the resin 5 is increased.Finally, in the measuring section, the spiral groove 3 is made into a uniform shallow groove, and the resin flows along this narrow flow path. The resin is uniformly kneaded and melted, the resin pressure is maintained at a desired pressure, the resin is measured, and the resin is extruded from a die (not shown) provided at the tip. Therefore, the extrusion rate of this type of extruder is determined by the shallow part of the helical groove 3, and if the depth of the groove in this area is made deeper, the extrusion rate can be increased even with the same size screw, but then The following problems arise. The bulk specific gravity of the resin is different between the solid state and the molten state, and the latter is larger, so if the depth of the groove at the screw tip is deepened, the resin will be extruded from the screw tip faster. , a part where the resin is not clogged occurs in the middle of the screw, causing unstable extrusion. Furthermore, when trying to extrude a large amount of resin using a screw having such a shallow groove portion, a large amount of frictional heat is generated due to shearing of the resin, making it difficult to control the resin temperature. Therefore, should I use a larger extruder to increase the amount of extrusion? 5. A forced cooling device is added, but the equipment cost increases, and in the latter case in particular, the low thermal conductivity of the resin causes local heating, which adversely affects extrusion performance. In view of this, the present invention has a supply section that is supplied with thermoplastic resin, a compression section that increases the pressure of the resin transferred from the supply section, and a metering section that measures the amount of resin to be extruded. In the screw unit installed in the barrel of the extruder with On the contrary, the core of the screw is made to have a uniform thickness in the supply section, compression section, and metering section.

すなわち、本発明においてはスクリユ一の供給部と圧縮
部は同一形状である。これを図に示す実施例に基いて詳
細に説明すれば、第1図に}いて1はスクリユ一の芯体
を示し、この芯体1に樹脂送り用のフライト2を設け、
フライト2で構成されるらせん溝3により熱可塑性樹脂
が移送され、加熱混練されるのであるがこのようなスク
リユ一の計量部には逆向きのフライト4が設けてあり、
これが樹脂の移送に対する抵抗部分となり、樹脂の発熱
を押えつつ、樹脂の押出量を増大できるのであるo例え
ばP=65mmφ、L/D=25(ここでDはスクリユ
一の直径、Lは長さを示す)のスクリユ一で基部のらせ
ん溝の深さ10m7!L.計量部の溝の深さ3.5m1
Lの従来の押出機では毎分50回程度の回転で、樹脂温
度は限定温度より15〜20℃も高かつた。これに対し
同寸法の本発明のスクリユ一で溝の深さはすべて10m
m1先端部に5ターン分の逆向きのフライトを設けたも
ので毎分50回程度の回転(略同じ押出量)では5〜1
0℃程度の温度上昇であり1毎分70回まで回転数を上
げても10〜20℃程度の温度上昇で済み、温度上昇を
同一とすれば、本発明によるスクリユ一の方が押出量を
増大させ得ることが判る。なお前述の実施例ではらせん
溝の深さの一定のもの即ち芯体の径を一様としたもので
逆向きのフライトも一条のらせん体によるものを示した
が、二条、三条と複数条のものにすれば抵抗部分として
の効果が更に向上する。また逆向きのフライトの長さは
樹脂の圧力及び流冊に応じ適宜撰定する。更に第2図は
ベント型押出機のスクリユ一に適用した場合を示し、樹
脂供給側からベント部5まではスクリユ一の芯体1の径
を一様にして溝3の深さを一様にし、ベント部5の手前
、すなわち樹脂供給側の計量部において逆向きのフライ
ト4を設けている。このようなベント型押出機のスクリ
ユ一では上流側(=樹脂供給側)と下流側とにそれぞれ
供給部、圧縮部、}よび計量部が設けられている。樹脂
はベント部5に対して上流側の供給部、圧縮部、ち・よ
び計量部においてそれぞれ供給、圧縮、および計量され
てからベント部5へ至り、下流側の供給部としてのベン
ト部5において発泡剤等の注入剤が新たに注入された後
、この注入剤と樹脂とが下流側の圧縮部訃よび計量部に
おいてそれぞれ圧縮、計量される。下流側の圧縮部およ
び計量部は従来と同様、溝を浅くしてある。この実施例
ではベント部5への樹脂の押出量を増大させることがで
きる。以上説明したように本発明によればバレル内に設
けたスクリユ一の先端部付近に逆向きのフライトを設け
これをスクリユ一による樹脂移送の抵抗として作用させ
たので、スクリユ一計量部の溝深さを従来のスクリユ一
より深くすることができ、したがつて、従来のスクリユ
一に比較するとL/Dが同じでも樹脂の発熱を抑えつつ
押出量を増大させることができる。
That is, in the present invention, the supply section and the compression section of the screw have the same shape. This will be explained in detail based on the embodiment shown in the drawings. In FIG.
The thermoplastic resin is transferred through the spiral groove 3 made up of flights 2 and heated and kneaded, but the measuring section of such a screw is provided with flights 4 facing in the opposite direction.
This becomes a resistance part to the transfer of the resin, and it is possible to increase the amount of resin extruded while suppressing the heat generation of the resin. For example, P = 65 mmφ, L/D = 25 (here, D is the diameter of the screw, and L is the length. ) The depth of the spiral groove at the base is 10m7! L. Measuring section groove depth 3.5m1
L's conventional extruder rotated about 50 times per minute, and the resin temperature was 15 to 20°C higher than the limiting temperature. In contrast, the depth of the grooves in the screws of the present invention having the same dimensions is all 10 m.
m1 has a flight in the opposite direction for 5 turns at the tip, and at a rotation rate of about 50 times per minute (approximately the same extrusion amount), 5 to 1
The temperature rise is about 0℃, and even if the rotation speed is increased to 70 times per minute, the temperature rise is only about 10 to 20℃.If the temperature rise is the same, the screw according to the present invention has a higher extrusion rate. It turns out that it can be increased. In the above-mentioned embodiments, the depth of the spiral groove is constant, that is, the diameter of the core body is uniform, and the flight in the opposite direction is also a one-threaded spiral. If it is made more effective, the effect as a resistor part will be further improved. In addition, the length of the flight in the opposite direction is appropriately selected depending on the pressure and flow rate of the resin. Furthermore, Fig. 2 shows a case where the screw is applied to a screw of a vent type extruder, and the diameter of the core 1 of the screw is uniform and the depth of the groove 3 is uniform from the resin supply side to the vent part 5. In front of the vent part 5, that is, in the measuring part on the resin supply side, a flight 4 facing in the opposite direction is provided. The screw of such a vented extruder is provided with a supply section, a compression section, and a metering section on the upstream side (=resin supply side) and downstream side, respectively. The resin is supplied, compressed, and measured in a supply section, a compression section, and a metering section on the upstream side of the vent section 5, and then reaches the vent section 5, and then in the vent section 5 as a supply section on the downstream side. After a new injection agent such as a foaming agent is injected, the injection agent and resin are compressed and measured in a compression section and a metering section on the downstream side, respectively. The compression section and metering section on the downstream side have shallow grooves, as in the conventional case. In this embodiment, the amount of resin extruded into the vent portion 5 can be increased. As explained above, according to the present invention, a flight in the opposite direction is provided near the tip of the screw provided in the barrel, and this acts as a resistance to the transfer of resin by the screw, so that the groove depth of the measuring portion of the screw is increased. It is possible to make the screw depth deeper than that of a conventional screw, and therefore, compared to a conventional screw, it is possible to increase the extrusion amount while suppressing heat generation of the resin even if the L/D is the same.

また本発明ではスクリユ一の芯体を供給部、圧縮部、於
よび計量部において一様な太さとしたので、計量部の溝
の深さが深くなるとともに、設計、製造が容易となる。
Further, in the present invention, the core of the screw has a uniform thickness in the supply section, compression section, and metering section, so that the depth of the groove in the metering section becomes deep and design and manufacturing are facilitated.

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

第1図及び第2図は本発明になる押出機用スクリユ一の
異なる実施例を示す側面図、第3図は従来の押出機用ス
クリユ一の側面図である。 1・・・スクリユ一芯体、2・・・フライト、3・・・
らせん溝、4・・・逆向きのフライト。
1 and 2 are side views showing different embodiments of a screw for an extruder according to the present invention, and FIG. 3 is a side view of a conventional screw for an extruder. 1... Screw one-core body, 2... Flight, 3...
Spiral groove, 4...Reverse flight.

Claims (1)

【特許請求の範囲】 1 熱可塑性樹脂を供給される供給部とこの供給部から
の移送されてくる樹脂の圧力を高める圧縮部との樹脂の
押出量を計量する計量部とを軸線方向へ順番に有し押出
機のバレル内に設置されるスクリューにおいて、計量部
における樹脂送り用フライトの向きを供給部および圧縮
部における樹脂送り用フライトの向きとは逆にし、スク
リューの芯体を供給部、圧縮部および計量部において一
様な太さとしたことを特徴とする押出機用スクリュー。 2 スクリューの計量部に設けた逆向きのフライトを複
数条としたことを特徴とする特許請求の範囲第1項記載
の押出機用スクリュー。
[Scope of Claims] 1. A supply section that is supplied with thermoplastic resin, a compression section that increases the pressure of the resin transferred from this supply section, and a measurement section that measures the amount of resin to be extruded, in order in the axial direction. In the screw installed in the barrel of the extruder, the direction of the resin feeding flight in the metering section is opposite to the direction of the resin feeding flight in the feeding section and the compression section, and the core of the screw is set in the feeding section, A screw for an extruder characterized by having a uniform thickness in a compression section and a metering section. 2. The screw for an extruder according to claim 1, characterized in that a plurality of flights in opposite directions are provided in the measuring section of the screw.
JP51028651A 1976-03-18 1976-03-18 Screw for extruder Expired JPS5913336B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP51028651A JPS5913336B2 (en) 1976-03-18 1976-03-18 Screw for extruder

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP51028651A JPS5913336B2 (en) 1976-03-18 1976-03-18 Screw for extruder

Publications (2)

Publication Number Publication Date
JPS52112655A JPS52112655A (en) 1977-09-21
JPS5913336B2 true JPS5913336B2 (en) 1984-03-29

Family

ID=12254404

Family Applications (1)

Application Number Title Priority Date Filing Date
JP51028651A Expired JPS5913336B2 (en) 1976-03-18 1976-03-18 Screw for extruder

Country Status (1)

Country Link
JP (1) JPS5913336B2 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US10328932B2 (en) 2014-06-02 2019-06-25 Magna Electronics Inc. Parking assist system with annotated map generation

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS50115270A (en) * 1974-02-26 1975-09-09
JPS50140563A (en) * 1974-05-01 1975-11-11

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS50115270A (en) * 1974-02-26 1975-09-09
JPS50140563A (en) * 1974-05-01 1975-11-11

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US10328932B2 (en) 2014-06-02 2019-06-25 Magna Electronics Inc. Parking assist system with annotated map generation

Also Published As

Publication number Publication date
JPS52112655A (en) 1977-09-21

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