JPS5937217B2 - Two-stage continuous kneading and extrusion equipment - Google Patents
Two-stage continuous kneading and extrusion equipmentInfo
- Publication number
- JPS5937217B2 JPS5937217B2 JP56083834A JP8383481A JPS5937217B2 JP S5937217 B2 JPS5937217 B2 JP S5937217B2 JP 56083834 A JP56083834 A JP 56083834A JP 8383481 A JP8383481 A JP 8383481A JP S5937217 B2 JPS5937217 B2 JP S5937217B2
- Authority
- JP
- Japan
- Prior art keywords
- extrusion
- kneading
- continuous kneading
- stage continuous
- 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
Links
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C48/00—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
- B29C48/25—Component parts, details or accessories; Auxiliary operations
- B29C48/36—Means for plasticising or homogenising the moulding material or forcing it through the nozzle or die
- B29C48/50—Details of extruders
- B29C48/505—Screws
- B29C48/67—Screws having incorporated mixing devices not provided for in groups B29C48/52 - B29C48/66
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C48/00—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
- B29C48/25—Component parts, details or accessories; Auxiliary operations
- B29C48/36—Means for plasticising or homogenising the moulding material or forcing it through the nozzle or die
- B29C48/365—Means for plasticising or homogenising the moulding material or forcing it through the nozzle or die using pumps, e.g. piston pumps
- B29C48/37—Gear pumps
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C48/00—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
- B29C48/25—Component parts, details or accessories; Auxiliary operations
- B29C48/36—Means for plasticising or homogenising the moulding material or forcing it through the nozzle or die
- B29C48/375—Plasticisers, homogenisers or feeders comprising two or more stages
- B29C48/385—Plasticisers, homogenisers or feeders comprising two or more stages using two or more serially arranged screws in separate barrels
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C48/00—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
- B29C48/25—Component parts, details or accessories; Auxiliary operations
- B29C48/36—Means for plasticising or homogenising the moulding material or forcing it through the nozzle or die
- B29C48/375—Plasticisers, homogenisers or feeders comprising two or more stages
- B29C48/387—Plasticisers, homogenisers or feeders comprising two or more stages using a screw extruder and a gear pump
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C48/00—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
- B29C48/25—Component parts, details or accessories; Auxiliary operations
- B29C48/36—Means for plasticising or homogenising the moulding material or forcing it through the nozzle or die
- B29C48/395—Means for plasticising or homogenising the moulding material or forcing it through the nozzle or die using screws surrounded by a cooperating barrel, e.g. single screw extruders
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C48/00—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
- B29C48/25—Component parts, details or accessories; Auxiliary operations
- B29C48/36—Means for plasticising or homogenising the moulding material or forcing it through the nozzle or die
- B29C48/50—Details of extruders
- B29C48/505—Screws
- B29C48/52—Screws with an outer diameter varying along the longitudinal axis, e.g. for obtaining different thread clearance
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C48/00—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
- B29C48/25—Component parts, details or accessories; Auxiliary operations
- B29C48/36—Means for plasticising or homogenising the moulding material or forcing it through the nozzle or die
- B29C48/50—Details of extruders
- B29C48/505—Screws
- B29C48/535—Screws with thread pitch varying along the longitudinal axis
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C48/00—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
- B29C48/25—Component parts, details or accessories; Auxiliary operations
- B29C48/92—Measuring, controlling or regulating
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C2948/00—Indexing scheme relating to extrusion moulding
- B29C2948/92—Measuring, controlling or regulating
- B29C2948/92504—Controlled parameter
- B29C2948/92514—Pressure
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C2948/00—Indexing scheme relating to extrusion moulding
- B29C2948/92—Measuring, controlling or regulating
- B29C2948/92819—Location or phase of control
- B29C2948/92857—Extrusion unit
- B29C2948/92876—Feeding, melting, plasticising or pumping zones, e.g. the melt itself
- B29C2948/92885—Screw or gear
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C48/00—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
- B29C48/03—Extrusion 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
- B29C48/04—Particle-shaped
Landscapes
- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- Extrusion Moulding Of Plastics Or The Like (AREA)
Description
【発明の詳細な説明】
本発明は、高分子材料の溶融、混線及び押出成形(又は
造粒化)を連続的に行なう2段型連続混練押出装置に関
するものである。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a two-stage continuous kneading and extrusion apparatus that continuously performs melting, mixing, and extrusion molding (or granulation) of a polymeric material.
従来の2段型連続混練押出装置としては第1図に示すよ
うなものがある。A conventional two-stage continuous kneading and extrusion apparatus is shown in FIG.
この2段型連続混練押出装置は、連続式混線機1と、こ
れにシュート2を介して連結されたスクリュ式押出成形
機3とから成っていた。This two-stage continuous kneading and extrusion apparatus consisted of a continuous mixer 1 and a screw extruder 3 connected to this through a chute 2.
連続式混練機1は、原料供給用のホッパー4を備えた混
練シリンダ5と、混練シリンダ5内に装入された2軸の
混練ロータ6とを有しており、混練ロータ6はモータ7
によって減速機8を介して駆動されるようにしである。The continuous kneading machine 1 has a kneading cylinder 5 equipped with a hopper 4 for supplying raw materials, and a two-shaft kneading rotor 6 inserted into the kneading cylinder 5. The kneading rotor 6 is connected to a motor 7.
It is designed to be driven by a speed reducer 8.
混線シリンダ5の先端側には混練度調節用のスロット9
が形成してあり、このスロット9によって混練度を調節
された溶融樹脂がシュート2に吐出されるようにしであ
る。There is a slot 9 on the tip side of the mixing cylinder 5 for adjusting the mixing degree.
is formed, and the molten resin whose kneading degree is adjusted by this slot 9 is discharged into the chute 2.
スクリュ式押出成形機3は、加熱装置付きのシリンダ1
0と、シリンダ10内に装入された単軸スクリュ11と
を有しており、単軸スクリュ11は減速機12を介して
モータ13によって駆動されるようにしである。The screw type extrusion molding machine 3 has a cylinder 1 equipped with a heating device.
0 and a single screw 11 inserted into a cylinder 10, and the single screw 11 is driven by a motor 13 via a speed reducer 12.
シリンダ10の先端側にばスクリーン14及びダイ15
が設けてあり、更にその前方にはダイ15から押出され
た樹脂を切断する水中カッタ16が設けられている。A screen 14 and a die 15 are provided on the tip side of the cylinder 10.
An underwater cutter 16 for cutting the resin extruded from the die 15 is further provided in front of the cutter.
ホッパ4から連続式混練機1のシリンダ5内に投入され
た樹脂原料は、ロータ6の回転によって溶融・混練され
、スロット9の開度によって混練度を調節され、棒状の
溶融樹脂とされてシュート2に吐出される。The resin raw material fed into the cylinder 5 of the continuous kneader 1 from the hopper 4 is melted and kneaded by the rotation of the rotor 6, the degree of kneading is adjusted by the opening degree of the slot 9, and it is turned into a rod-shaped molten resin and shot. 2.
棒状の溶融樹脂はスクリュ式押出機3に供給され、単軸
スクリュ11によって押出力を与えられて、スクリーン
14及びダイ15を通して押出され、水中カッタ16に
よって切断されて造粒される。The rod-shaped molten resin is supplied to a screw extruder 3, is given an extrusion force by a single screw 11, is extruded through a screen 14 and a die 15, is cut by an underwater cutter 16, and is granulated.
しかしながら、上記のような従来の2段型連続混練押出
装置では、スクリュ式押出機3における押出しに必要な
押出圧力(50〜250kg/c111)を単軸スクリ
ュ11の回転により与えるようにしてあったため、単軸
スクリュ11の直径に対する長さの比を10〜13と大
きくする必要があり、またシリンダ10は高圧の押出圧
力に耐えることができるようにする必要があり、このた
めスクリュ式押出成形機が大型化すると共に価格が高く
なり、しかも押出しのために多大なエネルギーを消費す
るという問題点があった。However, in the conventional two-stage continuous kneading and extrusion apparatus as described above, the extrusion pressure (50 to 250 kg/c111) required for extrusion in the screw extruder 3 was applied by rotating the single screw 11. , the ratio of the length to the diameter of the single screw 11 needs to be as large as 10 to 13, and the cylinder 10 needs to be able to withstand high extrusion pressure. However, as the size increases, the price increases, and extrusion consumes a large amount of energy.
本発明は、従来の2段型連続混練押出装置における上記
のような問題点を解消して、小型で価格が安く且つ消費
エネルギーの少ない2段型連続混練押出装置を得ること
を目的とするものである。The object of the present invention is to solve the above-mentioned problems in the conventional two-stage continuous kneading and extrusion device, and to obtain a two-stage continuous kneading and extrusion device that is small, inexpensive, and consumes less energy. It is.
以下、本発明をその実施例を示す添付図面の第2図に基
づいて説明する。Hereinafter, the present invention will be explained based on FIG. 2 of the accompanying drawings showing an embodiment thereof.
本発明による2段型連続混練押出装置は、連続式混練機
21と、これにシュート22を介して連結された押出成
形装置23とから成っている。The two-stage continuous kneading and extrusion apparatus according to the present invention comprises a continuous kneading machine 21 and an extrusion molding apparatus 23 connected to the continuous kneading machine 21 via a chute 22.
連続式混線機21は、原料供給用のホッパー24を備え
た混練シリンダ25と、混練シリンダ25内に装入され
た2軸の混練ロータ26とを有しており、混練ロータ2
6はモータ27によって減速機28を介して駆動される
ようにしである。The continuous mixer 21 has a kneading cylinder 25 equipped with a hopper 24 for supplying raw materials, and a two-shaft kneading rotor 26 inserted into the kneading cylinder 25.
6 is designed to be driven by a motor 27 via a reduction gear 28.
混線シリンダ25の先端側には混練度調節用のスロット
29が形成してあり、このスロット29によって混練度
を調節された溶融樹脂がシュート22に吐出されるよう
にしである。A slot 29 for adjusting the kneading degree is formed at the tip side of the mixing cylinder 25, and the molten resin whose kneading degree is adjusted by the slot 29 is discharged into the chute 22.
押出成形装置23はスクリュ式押出機30と、これの先
端圧出部に連結したギアポンプ31と、ギアポンプ31
の吐出部に設けたダイ32とを有している。The extrusion molding device 23 includes a screw type extruder 30, a gear pump 31 connected to the extruding end of the extruder 30, and a gear pump 31.
It has a die 32 provided at the discharge part of the discharge part.
スクリュ式押出機30は、加熱装置付きのシリンダ33
と、シリンダ33内に装入された単軸スクリュ34とを
有しており、単軸スクリュ34は減速機35を介してモ
ータ36によって駆動されるようにしである。The screw extruder 30 has a cylinder 33 equipped with a heating device.
and a single-shaft screw 34 inserted into a cylinder 33, and the single-shaft screw 34 is driven by a motor 36 via a reduction gear 35.
単軸スクリュ34は直径に対する長さの比は4〜6とし
てその長さを短かくしてあり、またシリンダ33は数k
g/critの圧力に耐えることができる程度の構造に
しである。The single screw 34 has a short length to diameter ratio of 4 to 6, and the cylinder 33 has a length of several kilometres.
The structure is such that it can withstand pressure of g/crit.
スクリュ式押出機30の先端圧出部には2つの歯車37
及び38をかみ合わせて成るギアポンプ31が設けてあ
り、ギアポンプ31は図示してない変速操作可能な駆動
装置によって駆動されるようにしである。There are two gears 37 at the tip extrusion part of the screw extruder 30.
and 38 are provided, and the gear pump 31 is driven by a drive device (not shown) capable of variable speed operation.
ギアポンプ31の吐出部前方にはスクリーン39及びダ
イ32が設けてあり、更にその前方にはダイ32から押
出された樹脂を切断する水中カッタ40が設けである。A screen 39 and a die 32 are provided in front of the discharge portion of the gear pump 31, and an underwater cutter 40 for cutting the resin extruded from the die 32 is further provided in front of the screen 39 and die 32.
次に、上記のような構成を有する本発明による2段型連
続混練押出装置の作用について説明する。Next, the operation of the two-stage continuous kneading and extrusion apparatus according to the present invention having the above-mentioned configuration will be explained.
ホッパ24から連続式混線機21のシリンダ25内に投
入された樹脂原料は、ロータ26の回転によって溶融・
混練され、スロット29の開度によって混練度を調節さ
れ、棒状の溶融樹脂とされてシュート22に吐出される
。The resin raw material put into the cylinder 25 of the continuous mixer 21 from the hopper 24 is melted and melted by the rotation of the rotor 26.
The resin is kneaded, the degree of kneading is adjusted by the opening degree of the slot 29, and the molten resin is discharged into the chute 22 as a rod-shaped molten resin.
棒状の溶融樹脂はスクリュ式押出機30に供給され、ス
クリュ34によって数に9/crj、程度の圧力を加え
た状態でギアポンプ31へ圧出される。The rod-shaped molten resin is supplied to a screw extruder 30, and is forced out by a screw 34 to a gear pump 31 under pressure of about 9/crj.
次いで、溶融樹脂はギアポンプ31によって50〜25
0 kg/iの押出圧力に昇圧されてスクリーン39及
びダイ32を通して押出され、水中カッタ40によって
切断されて造粒される。Next, the molten resin is pumped by the gear pump 31 to
The extrusion pressure is increased to 0 kg/i, extruded through a screen 39 and die 32, cut by an underwater cutter 40, and granulated.
以上説明してきたように、本発明によると、連続式混練
機と、これにシュートを介して連結された押出成形装置
とから成る2段型連続混練押出装置における押出成形装
置を、スクリュ式押出機と、スクリュ式押出機の先端圧
出部に連結したギアポンプと、ギアポンプ吐出部に設け
たダイとから構成したので、スクリュ式押出機の圧出部
の圧力を数kg/cyytとすることができることとな
り、スクリュの長さを従来のものの1/2〜1/3とす
ることができると共にシリンダの肉厚も薄くすることが
できる。As explained above, according to the present invention, the extrusion molding device in a two-stage continuous kneading and extrusion device consisting of a continuous kneading machine and an extrusion molding device connected thereto via a chute can be replaced with a screw type extruder. Since it is composed of a gear pump connected to the extrusion section at the tip of the screw extruder and a die provided at the discharge section of the gear pump, the pressure at the extrusion section of the screw extruder can be reduced to several kg/cyyt. Therefore, the length of the screw can be reduced to 1/2 to 1/3 of that of the conventional screw, and the wall thickness of the cylinder can also be reduced.
これに加えてスクリュ駆動用のモータ及び減速機も小型
化することができ、結局、押出機を小型化して価格を低
減することができる。In addition, the screw driving motor and speed reducer can also be downsized, and as a result, the extruder can be downsized and the cost can be reduced.
従って、押出機の消費エネルギーは大幅に減少し、従来
のものの1/2〜115とすることができる。Therefore, the energy consumption of the extruder is significantly reduced, and can be reduced to 1/2 to 115 times that of conventional extruders.
また、スクリュによるせん新作用が小さくな、るため樹
脂温度の上昇を防止することができ、樹脂の物性低下を
生じることがなくなり高品質の樹脂を得ることができる
。Furthermore, since the shearing effect of the screw is reduced, an increase in resin temperature can be prevented, and a high quality resin can be obtained without deterioration of the physical properties of the resin.
第1図は従来の2段型連続混練押出装置の断面図、第2
図は本発明による2段型連続混練押出装置の断面図であ
る。
21・・・・・・連続式混練機、22・・・・・・シュ
ート、23・・・・・・押出成形装置、30・・・・・
・スクリュ式押出機、31・・・・・・ギアポンプ、3
2・・・・・・ダイ。Figure 1 is a cross-sectional view of a conventional two-stage continuous kneading and extrusion device;
The figure is a sectional view of a two-stage continuous kneading and extrusion device according to the present invention. 21... Continuous kneading machine, 22... Chute, 23... Extrusion molding device, 30...
・Screw extruder, 31...Gear pump, 3
2...Die.
Claims (1)
た押出成形装置とから成る2段型連続混練押出装置にお
いて、 押出成型装置が、スクリュ式押出機と、スクリュ式押出
機の先端圧出部に連結したギアポンプと、ギアポンプ吐
出部に設けたダイとを有することを特徴とする2段型連
続混練押出装置。[Claims] 1. A two-stage continuous kneading and extrusion device comprising a continuous mixing machine and an extrusion molding device connected thereto via a chute, wherein the extrusion molding device includes a screw type extruder and a screw type extruder. A two-stage continuous kneading and extrusion device characterized by having a gear pump connected to a tip extrusion section of an extruder, and a die provided at the gear pump discharge section.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP56083834A JPS5937217B2 (en) | 1981-06-02 | 1981-06-02 | Two-stage continuous kneading and extrusion equipment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP56083834A JPS5937217B2 (en) | 1981-06-02 | 1981-06-02 | Two-stage continuous kneading and extrusion equipment |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS57199638A JPS57199638A (en) | 1982-12-07 |
| JPS5937217B2 true JPS5937217B2 (en) | 1984-09-08 |
Family
ID=13813720
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP56083834A Expired JPS5937217B2 (en) | 1981-06-02 | 1981-06-02 | Two-stage continuous kneading and extrusion equipment |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS5937217B2 (en) |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH11268033A (en) * | 1998-03-24 | 1999-10-05 | Japan Steel Works Ltd:The | Twin screw extruder |
-
1981
- 1981-06-02 JP JP56083834A patent/JPS5937217B2/en not_active Expired
Also Published As
| Publication number | Publication date |
|---|---|
| JPS57199638A (en) | 1982-12-07 |
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