JPS6335403B2 - - Google Patents

Info

Publication number
JPS6335403B2
JPS6335403B2 JP59137488A JP13748884A JPS6335403B2 JP S6335403 B2 JPS6335403 B2 JP S6335403B2 JP 59137488 A JP59137488 A JP 59137488A JP 13748884 A JP13748884 A JP 13748884A JP S6335403 B2 JPS6335403 B2 JP S6335403B2
Authority
JP
Japan
Prior art keywords
flight
valley
valleys
outer diameter
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.)
Expired
Application number
JP59137488A
Other languages
Japanese (ja)
Other versions
JPS6116812A (en
Inventor
Kenji Nozawa
Akikuni Ide
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.)
Shibaura Machine Co Ltd
Original Assignee
Toshiba Machine 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 Toshiba Machine Co Ltd filed Critical Toshiba Machine Co Ltd
Priority to JP59137488A priority Critical patent/JPS6116812A/en
Publication of JPS6116812A publication Critical patent/JPS6116812A/en
Publication of JPS6335403B2 publication Critical patent/JPS6335403B2/ja
Granted legal-status Critical Current

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29BPREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
    • B29B7/00Mixing; Kneading
    • B29B7/30Mixing; Kneading continuous, with mechanical mixing or kneading devices
    • B29B7/34Mixing; Kneading continuous, with mechanical mixing or kneading devices with movable mixing or kneading devices
    • B29B7/38Mixing; Kneading continuous, with mechanical mixing or kneading devices with movable mixing or kneading devices rotary
    • B29B7/40Mixing; Kneading continuous, with mechanical mixing or kneading devices with movable mixing or kneading devices rotary with single shaft
    • B29B7/42Mixing; Kneading continuous, with mechanical mixing or kneading devices with movable mixing or kneading devices rotary with single shaft with screw or helix
    • B29B7/428Parts or accessories, e.g. casings, feeding or discharging means
    • B29B7/429Screws
    • 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
    • B29C48/62Screws characterised by the shape of the thread channel, e.g. U-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

Landscapes

  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (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)

Description

【発明の詳細な説明】 〔発明の属する技術分野〕 本発明は熱可塑性樹脂を成形する押出機や射出
成形機或いは吹込成形機等(以下これらを成形機
という)のスクリユに関する。
DETAILED DESCRIPTION OF THE INVENTION [Technical field to which the invention pertains] The present invention relates to a screw for an extruder, injection molding machine, blow molding machine, or the like (hereinafter referred to as a molding machine) for molding a thermoplastic resin.

成形機においてスクリユによる樹脂の混練およ
び混合は極めて重要であり、これが不充分である
と成形品は不均質になつて特性が劣り不良品にな
る。なお混練とは樹脂材料であるペレツトに圧縮
力が作用して剪断力により溶融化することをい
い、混合とは溶融したものと未溶融のものをまぜ
あわせることを指すものとする。
Kneading and mixing of the resin using a screw in a molding machine is extremely important, and if this is insufficient, the molded product will be non-uniform and have poor properties, resulting in a defective product. Note that kneading refers to melting the resin material pellets by compressive force and shearing force, and mixing refers to mixing molten and unmolten materials.

〔従来技術〕[Prior art]

混練および混合を良くするため従来から第1図
および第2図に示すように、スクリユ11の1ピ
ツチ間に互に逆位相に配置した2個の偏心リング
である谷部12および13を設ける方式が提案さ
れている。この方式において谷部12のシリンダ
14に対する深い側の隙間15から浅い側の隙間
16にペレツトが移動するとき、圧縮力は作用す
るが2つの谷部12と13との間に山部がないの
で、一側の谷12が浅くなりシリンダ14と谷部
12とのクサビ効果により混練しようとしても、
隙間が深くて抵抗の少い他側の谷部13へペレツ
トは流れてほとんど混練されなかつた。
In order to improve kneading and mixing, as shown in FIGS. 1 and 2, conventionally, two eccentric rings 12 and 13, which are eccentric rings arranged in opposite phases, are provided between one pitch of the screw 11. is proposed. In this method, when the pellet moves from the gap 15 on the deep side to the gap 16 on the shallow side of the cylinder 14 in the trough 12, compressive force acts, but there is no peak between the two troughs 12 and 13. , even if the valley 12 on one side becomes shallower and kneading is attempted due to the wedge effect between the cylinder 14 and the valley 12,
The pellets flowed to the valley part 13 on the other side where the gap was deep and there was less resistance, and the pellets were hardly mixed.

〔発明の目的〕[Purpose of the invention]

本発明はこのような欠点を除去したものでその
目的は、第1フライトとこのフライトの間にその
外径より小さい第2および第3フライトを配置
し、これらのフライトにより形成された谷部にお
いて中央の谷と左右の谷を逆位相の偏心円にする
ことにより、各谷において深い谷から浅い谷へペ
レツトが移動するときクサビ効果の強い圧縮力に
より確実な混練を行うようにすると共に、混練さ
れて溶融した樹脂は浅い谷から他側の深い谷に第
2および第3フライトを超えて強制的に移動させ
ることにより混合させ、もつと混練と混合を効率
よく行うようにした熱可塑性樹脂高混練スクリユ
を提供することにある。
The present invention eliminates such drawbacks, and its purpose is to arrange second and third flights smaller than the outer diameter of the first flight and the second and third flights between the first flight and the first flight, and in the valley formed by these flights. By making the center valley and the left and right valleys eccentric circles with opposite phases, when the pellets move from deep to shallow valleys in each valley, the strong compressive force of the wedge effect ensures reliable kneading. The molten resin is mixed by forcibly moving from a shallow valley to a deep valley on the other side over the second and third flights. Our purpose is to provide kneading screws.

〔発明の要点〕[Key points of the invention]

本発明の熱可塑性樹脂高混練スクリユは第1フ
ライトと、第1フライトの1ピツチ間に形成され
かつ第1フライトの外径より小さい外径にした第
2フライトおよび第3フライトと、3箇のフライ
トにより形成されその中央の谷部および左右の谷
部はそれぞれスクリユ軸心に対し逆位相の偏心円
でありかつ左右谷部の流路断面積の和は中央谷部
の流路断面積にほぼ等しくした3箇の谷部とから
なることを特徴にしている。
The thermoplastic resin high kneading screw of the present invention has a first flight, a second flight and a third flight formed between one pitch of the first flight and having an outer diameter smaller than the outer diameter of the first flight, and three flights. Formed by the flight, the central trough and left and right troughs are eccentric circles with opposite phases to the screw axis, and the sum of the flow passage cross-sectional areas of the left and right valleys is approximately equal to the flow passage cross-sectional area of the central trough. It is characterized by consisting of three equal valleys.

〔発明の実施例〕[Embodiments of the invention]

以下本発明について一実施例を示した第3図な
いし第8図について説明する。スクリユ31はそ
の第1フライト32の1ピツチ間に第1フライト
の外径より小さい外径の第2フライト33および
第3フライト34を有する3条スクリユであつ
て、これら3箇のフライト32ないし34により
中央の谷35ならびに左右の谷36および37が
形成されている。なお第1フライト32の外径は
シリンダ14の内径より僅かに小さい。谷35な
いし37は第4図および第5図に示すようにその
断面は円形をなしスクリユ31の軸心に対し偏心
しており、かつ谷35に対し谷36および37は
逆位相に配置されている。また各谷35ないし3
7の円形は同一直径であり、シリンダ14の内面
から谷底までの距離のうち最も浅い寸法をαとし
最も深い寸法をβとし、シリンダ14の内面から
第2フライト33および第3フライト34の頂部
間距離をγとする。αとγの関係はγαである
が、図ではγ>αの場合を示してある。
The present invention will be explained below with reference to FIGS. 3 to 8 showing one embodiment. The screw 31 is a three-thread screw having a second flight 33 and a third flight 34 having an outer diameter smaller than the outer diameter of the first flight between each pitch of the first flight 32, and these three flights 32 to 34 A central valley 35 and left and right valleys 36 and 37 are formed by this. Note that the outer diameter of the first flight 32 is slightly smaller than the inner diameter of the cylinder 14. As shown in FIGS. 4 and 5, the valleys 35 to 37 have circular cross sections and are eccentric to the axis of the screw 31, and the valleys 36 and 37 are arranged in opposite phases to the valley 35. . Also each valley 35 to 3
The circles 7 have the same diameter, the shallowest dimension of the distance from the inner surface of the cylinder 14 to the bottom of the valley is α, the deepest dimension is β, and the distance between the inner surface of the cylinder 14 and the top of the second flight 33 and the third flight 34 is Let the distance be γ. The relationship between α and γ is γα, but the figure shows the case where γ>α.

次に前述した実施例の動作を説明する。第1フ
ライト32の1ピツチ間内のペレツトに谷36お
よび37の谷深さがβからαに変るとき、同様に
谷35の谷深さがβからαに変るとき谷底とシリ
ンダ14とのクサビ効果により強い圧縮力を受け
て確実な混練を受ける。混練されて溶融した樹脂
は第2フライト33および第3フライト34の頂
部隙間γを強制的に超えされて、浅いα部から深
いβ部へ流れ各35と谷36および37の樹脂は
混合される。
Next, the operation of the embodiment described above will be explained. When the depth of the valleys 36 and 37 in the pellet within one pitch of the first flight 32 changes from β to α, and similarly when the depth of the valley 35 changes from β to α, the wedge between the valley bottom and the cylinder 14 Due to the effect, it receives strong compressive force and receives reliable kneading. The kneaded and melted resin is forced to cross the top gap γ of the second flight 33 and the third flight 34, and flows from the shallow α part to the deep β part, and the resins in each 35 and the valleys 36 and 37 are mixed. .

〔発明の効果〕〔Effect of the invention〕

本発明の熱可塑性樹脂高混練スクリユは以上説
明したように、第1フライトの1ピツチ間に第1
フライトより外径の小さい第2フライトおよび第
3フライトを有する3条スクリユであつて、この
3箇のフライトにより中央の谷と左右の谷とを形
成し、これらの谷は断面が円形でスクリユ軸心に
偏心すると共に中央の谷と左右の谷の偏心は逆位
相に配置した。またシリンダの内面から谷底まで
の距離のうち最も浅い寸法をαとし最も深い寸法
をβとし、シリンダ14の内面から第2フライト
および第3フライトの頂部間距離をγとした。
As explained above, the thermoplastic resin high kneading screw of the present invention has a first
It is a three-way screw having a second flight and a third flight with an outer diameter smaller than the flight, and these three flights form a central valley and left and right valleys, and these valleys have a circular cross section and are aligned with the screw axis. It is eccentric to the center, and the eccentricity of the center valley and the left and right valleys are arranged in opposite phases. Furthermore, among the distances from the inner surface of the cylinder to the bottom of the valley, the shallowest dimension was α, the deepest dimension was β, and the distance between the tops of the second and third flights from the inner surface of the cylinder 14 was γ.

この構成により第1フライト1ピツチ間のペレ
ツトは谷底からシリンダ内面までの谷深さがβか
らαに変るとき、クサビ効果の強い圧縮力により
確実な混練を受けると共に、混練されて溶融した
樹脂は第2フライトおよび第3フライトの頂部を
強制的に超えさせられて隙間の浅い方から深い方
へと隣の谷に移動して混合される。このとき一側
の谷深さが浅くなつて流路断面積が減少して圧力
P1は高く、他側の谷深さが深くなつて流路断面
積が増加して圧力P2は低いこと、ならびに両側
断面積の和は常にほぼ同じであるから混練されて
溶融した樹脂は円滑に第2フライトおよび第3フ
ライトを超えて混合される。
With this configuration, when the depth of the valley between the pitches of the first flight changes from β to α, the pellets are reliably kneaded by the strong compressive force of the wedge effect, and the kneaded and molten resin is It is forced to go over the tops of the second and third flights and moves from the shallower gap to the deeper one into the adjacent valley where it is mixed. At this time, the depth of the valley on one side becomes shallower, the cross-sectional area of the flow path decreases, and the pressure increases.
P1 is high, the depth of the trough on the other side becomes deeper, the cross-sectional area of the flow path increases, and the pressure P2 is low, and the sum of the cross-sectional areas on both sides is always almost the same, so the kneaded and melted resin will flow smoothly. Mixed over the second and third flights.

また3条スクリユにより流路内樹脂は1回の圧
縮で3分割されて効果的な混練を受ける。さらに
2条スクリユでは谷深さが浅くなつたとき溶融樹
脂は第2フライトの頂部を超え深い谷側に導かれ
るが、フライトによるせきが一方のみのためせき
と反対側の溶融樹脂は深い側に導かれず取り残さ
れて効率が落ちていた。本発明では第7図に示す
ように谷深さが浅くなると溶融樹脂は両側の深い
側に導かれるため効率は倍加する。さらに第8図
に示すように左右の谷内の溶融樹脂は中央の谷へ
両側から流れるため樹脂の混合がより高められる
等多くの利点を有する。この結果成形品の物性は
良く樹脂温も均一になつて均質な成形品が得られ
た。
Further, the resin in the channel is divided into three parts by one compression due to the three-thread screw, and is effectively kneaded. Furthermore, when the valley depth becomes shallow in the case of a two-thread screw, the molten resin passes over the top of the second flight and is guided to the deeper valley side, but since the weir by the flight is only on one side, the molten resin on the opposite side to the weir is guided to the deeper side. They were left behind without guidance, and their efficiency was declining. In the present invention, as shown in FIG. 7, when the valley depth becomes shallow, the molten resin is guided to the deeper sides on both sides, so the efficiency doubles. Furthermore, as shown in FIG. 8, since the molten resin in the left and right valleys flows from both sides to the central valley, there are many advantages such as improved mixing of the resins. As a result, the physical properties of the molded product were good, the resin temperature was uniform, and a homogeneous molded product was obtained.

なお3条スクリユより多条にしたときは樹脂の
分割は多くなるものの第1フライト1ピツチ間の
流路断面積が減少して好ましくなく、また流路断
面積を増加するため第1フライト1ピツチ間の距
離を大きくすると送り効率が減少して全体の効率
は低下することになる。
Note that when the number of threads is greater than three threads, the resin will be split more, but the cross-sectional area of the flow path between each pitch of the first flight will decrease, which is undesirable. Increasing the distance between them will reduce the feed efficiency and reduce the overall efficiency.

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

第1図は従来例の縦断面図、第2図は第1図の
2−2線断面図、第3図ないし第8図は本発明の
一実施例を示し、第3図は縦断面図、第4図は第
3図の4−4線断面図、第5図は第3図の5−5
線断面図、第6図は5−5線断面を展開した図、
第7図は第6図の7−7線断面図、第8図は第6
図の8−8線断面図を示す。 31……スクリユ、32……第1フライト、3
3……第2フライト、34……第3フライト、3
5……中央の谷、36……左側の谷、37……右
側の谷。
FIG. 1 is a longitudinal sectional view of a conventional example, FIG. 2 is a sectional view taken along line 2-2 in FIG. 1, and FIGS. 3 to 8 show an embodiment of the present invention. , Fig. 4 is a sectional view taken along line 4-4 in Fig. 3, and Fig. 5 is a sectional view taken along line 5-5 in Fig. 3.
Line sectional view, Figure 6 is an expanded view of the 5-5 line cross section,
Figure 7 is a sectional view taken along line 7-7 of Figure 6, and Figure 8 is a cross-sectional view of Figure 6.
A sectional view taken along line 8-8 in the figure is shown. 31... Skrill, 32... 1st flight, 3
3...Second flight, 34...Third flight, 3
5... Central valley, 36... Valley on the left, 37... Valley on the right.

Claims (1)

【特許請求の範囲】[Claims] 1 第1フライトと、同第1フライトの1ピツチ
間に形成されかつ同第1フライトの外径より小さ
い外径にした第2フライトおよび第3フライト
と、前記3箇のフライトにより形成されその中央
の谷部および左右の谷部はそれぞれスクリユ軸心
に対し逆位相の偏心円でありかつ前記左右谷部の
流路断面積の和は前記中央谷部の流路断面積にほ
ぼ等しくした3箇の谷部とからなり、それぞれの
前記谷部のシリンダ内面からの谷深さが最も浅い
寸法をαとし最も深い寸法をβとしたとき、前記
谷深さがαからβに変化する際前記左右の谷は同
一位相そして前記中央の谷はこれと逆位相で変化
することを特徴とする熱可塑性樹脂高混練スクリ
ユ。
1. A first flight, a second flight and a third flight that are formed between one pitch of the first flight and have an outer diameter smaller than the outer diameter of the first flight, and a flight that is formed by the three flights and the center thereof. The trough and the left and right troughs are eccentric circles with opposite phases with respect to the screw axis, and the sum of the flow passage cross-sectional areas of the left and right valleys is approximately equal to the flow passage cross-sectional area of the central trough. If the shallowest dimension of each valley depth from the inner surface of the cylinder is α and the deepest dimension is β, then when the valley depth changes from α to β, the left and right A highly kneaded thermoplastic resin screw, characterized in that the valleys in the center change in the same phase and the valley in the center changes in an opposite phase.
JP59137488A 1984-07-03 1984-07-03 Screw for highly kneading thermoplastic resin Granted JPS6116812A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP59137488A JPS6116812A (en) 1984-07-03 1984-07-03 Screw for highly kneading thermoplastic resin

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP59137488A JPS6116812A (en) 1984-07-03 1984-07-03 Screw for highly kneading thermoplastic resin

Publications (2)

Publication Number Publication Date
JPS6116812A JPS6116812A (en) 1986-01-24
JPS6335403B2 true JPS6335403B2 (en) 1988-07-14

Family

ID=15199812

Family Applications (1)

Application Number Title Priority Date Filing Date
JP59137488A Granted JPS6116812A (en) 1984-07-03 1984-07-03 Screw for highly kneading thermoplastic resin

Country Status (1)

Country Link
JP (1) JPS6116812A (en)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5342125A (en) * 1992-05-14 1994-08-30 Great Lakes Feedscrews, Inc. Feedscrew for injection molding and extrusion
CN104002447B (en) * 2014-05-15 2015-10-28 华南理工大学 A kind of eccentric rotor volume fluctuation deformation plasticizing transportation method and device

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS513186A (en) * 1974-06-24 1976-01-12 Matsushita Electric Ind Co Ltd

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS513186A (en) * 1974-06-24 1976-01-12 Matsushita Electric Ind Co Ltd

Also Published As

Publication number Publication date
JPS6116812A (en) 1986-01-24

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