JPH0337495B2 - - Google Patents
Info
- Publication number
- JPH0337495B2 JPH0337495B2 JP58043068A JP4306883A JPH0337495B2 JP H0337495 B2 JPH0337495 B2 JP H0337495B2 JP 58043068 A JP58043068 A JP 58043068A JP 4306883 A JP4306883 A JP 4306883A JP H0337495 B2 JPH0337495 B2 JP H0337495B2
- Authority
- JP
- Japan
- Prior art keywords
- flight
- clearance
- kneading
- dullage
- dalmage
- 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 - Lifetime
Links
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29B—PREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
- B29B7/00—Mixing; Kneading
- B29B7/30—Mixing; Kneading continuous, with mechanical mixing or kneading devices
- B29B7/34—Mixing; Kneading continuous, with mechanical mixing or kneading devices with movable mixing or kneading devices
- B29B7/38—Mixing; Kneading continuous, with mechanical mixing or kneading devices with movable mixing or kneading devices rotary
- B29B7/40—Mixing; Kneading continuous, with mechanical mixing or kneading devices with movable mixing or kneading devices rotary with single shaft
- B29B7/42—Mixing; Kneading continuous, with mechanical mixing or kneading devices with movable mixing or kneading devices rotary with single shaft with screw or helix
- B29B7/425—Mixing; Kneading continuous, with mechanical mixing or kneading devices with movable mixing or kneading devices rotary with single shaft with screw or helix with screw surrounded by a casing provided with grooves or cavities
-
- 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
- B29C48/56—Screws having grooves or cavities other than the thread or the channel
-
- 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
- B29C48/68—Barrels or cylinders
- B29C48/685—Barrels or cylinders characterised by their inner surfaces, e.g. having grooves, projections or threads
- B29C48/686—Barrels or cylinders characterised by their inner surfaces, e.g. having grooves, projections or threads having grooves or cavities
-
- 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
Landscapes
- Engineering & Computer Science (AREA)
- Mechanical Engineering (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】
本発明は樹脂の混練可塑化装置に関するもので
ある。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a resin kneading and plasticizing apparatus.
プラスチツク材料に各種フイラーを混入させ、
均質に分散させ、強度向上、寸法安定、コストダ
ウン、他材料の代替等の種々の目的を達成させる
方法としての複合成形は、射出成形による加工業
界において強く望まれている。 By mixing various fillers into plastic materials,
Composite molding is strongly desired in the injection molding processing industry as a method for homogeneously dispersing materials and achieving various objectives such as improving strength, dimensional stability, reducing costs, and substituting other materials.
複合射出成形においては、既に押出機或は混練
機によつてフイラーを充填混入した複合ペレツト
の使用による従来の方法でなく、フイラーとプラ
スチツク材料を射出成形機に直接供給して成形す
るダイレクトブレンド法が、コストダウン、省エ
ネルギ、省力化の目的に大きく寄与する。本目的
を達成する優れた技術に、特公昭56−47847号の
発明がある。 In composite injection molding, instead of the conventional method of using composite pellets that have already been filled and mixed with filler using an extruder or kneader, a direct blend method is used in which the filler and plastic material are directly fed to an injection molding machine and molded. This greatly contributes to the objectives of cost reduction, energy saving, and labor saving. An excellent technique for achieving this purpose is the invention disclosed in Japanese Patent Publication No. 47847/1983.
この技術はフイラーの分散混練に極めて優れた
技術ではあるが、可塑化能力が低下し、生産性の
向上が期待できないという欠点を有し、可塑化の
安定性にも若干欠くという欠点もある。 Although this technique is an extremely excellent technique for dispersing and kneading fillers, it has the disadvantage that the plasticizing ability is reduced and no improvement in productivity can be expected, and the stability of plasticization is also slightly lacking.
本発明は、これらの欠点を解消し、混練分散効
果に優れ、可塑化能力の低下を防ぎ、生産性の高
い複合成形も行える樹脂の混練可塑化装置を提供
するものである。 The present invention eliminates these drawbacks and provides a resin kneading and plasticizing apparatus that has excellent kneading and dispersion effects, prevents deterioration of plasticizing ability, and can perform composite molding with high productivity.
第1図は従来の技術(特公昭56−47847号)の
例で、加熱筒1の材料供給口2とベント孔3の間
に、材料供給ゾーン4、可塑化混練ゾーン5を設
け、加熱筒1の内部に軸方向に溝6を複数個設
け、一方、スクリユ7には、その可塑化混練ゾー
ン5に多条ねじ8を設けたものである。溝6や多
条ねじ8部の横断面を第2図に示す。第2図にお
いて、2点鎖線で示す矢印はスクリユ7の回転方
向を示し、実線の矢印は樹脂の流れ状態を示す。
第2図に示すように、多条ねじのフライト山9の
推進側10はスクリユ7の回転方向に直角に形成
してあり、フライト山9の推進側と反対側11は
徐々にスクリユ直径が小さくなるように形成して
ある。したがつて、多条ねじ溝空間12から加熱
筒1の溝6である溝空間13への材料の後方移動
は、スクリユ7が回転すると、加熱筒1とスクリ
ユ7の相対運動により行われる。即ち、展開図と
して示した第3図の如く、多条ねじ8のフライト
推進側10によつて前方へ移送されるべき樹脂材
料の一部は、フライト山9をのり越えて、加熱筒
1の軸方向溝空間13を経て後方の多条ねじ溝空
間12へ漏洩する。これが、混練分散が優れてい
る理由であるが、一方、可塑化能力の低下を生じ
ている理由でもある。又、更に、加熱筒1の軸方
向溝6が、可塑化混練ゾーン5又は材料供給口2
とベント孔3の間を複数個連続して連通している
ことが、加熱筒1内の圧力維持が難しく、低圧と
なり、フイラーの切断破損が少い優れた利点の理
由である一方、移送能力が不安定になる理由でも
ある。 Figure 1 shows an example of the conventional technology (Japanese Patent Publication No. 56-47847), in which a material supply zone 4 and a plasticization kneading zone 5 are provided between the material supply port 2 and the vent hole 3 of the heating cylinder 1. A plurality of grooves 6 are provided in the axial direction inside the screw 1, and a multi-thread screw 8 is provided in the plasticizing and kneading zone 5 of the screw 7. A cross section of the groove 6 and the multi-start thread 8 is shown in FIG. In FIG. 2, arrows shown by two-dot chain lines indicate the direction of rotation of the screw 7, and solid arrows indicate the flow state of the resin.
As shown in Fig. 2, the propulsion side 10 of the flight ridges 9 of the multi-thread screw is formed at right angles to the direction of rotation of the screw 7, and the screw diameter gradually decreases on the side 11 opposite to the propulsion side of the flight ridges 9. It is formed so that Therefore, the backward movement of the material from the multi-thread groove space 12 to the groove space 13, which is the groove 6 of the heating cylinder 1, is carried out by the relative movement between the heating cylinder 1 and the screw 7 when the screw 7 rotates. That is, as shown in FIG. 3, which is a developed view, a part of the resin material to be transferred forward by the flight propulsion side 10 of the multi-thread screw 8 climbs over the flight crest 9 and reaches the heating cylinder 1. It leaks through the axial groove space 13 to the rear multiple thread groove space 12 . This is the reason why the kneading and dispersion is excellent, but it is also the reason why the plasticizing ability is decreased. Furthermore, the axial groove 6 of the heating cylinder 1 is connected to the plasticization kneading zone 5 or the material supply port 2.
The fact that there is continuous communication between the vent hole 3 and the vent hole 3 is the reason why it is difficult to maintain the pressure inside the heating cylinder 1, resulting in a low pressure, which is an excellent advantage in that the filler is less likely to be cut and damaged. This is also the reason why it becomes unstable.
本発明は、これらの長所を維持しつつ、欠点を
なくし、より優れた装置を提供するものである。 The present invention maintains these advantages while eliminating the disadvantages and provides a superior device.
本発明では、そのために、樹脂の混練可塑化装
置において、加熱筒の可塑化混練ゾーンに、軸方
向に断続した凹部を加熱筒内面に複数個設け、ス
クリユの可塑化混練ゾーンに、単一もしくは複数
個のダルメージを有するダルメージ部を設けた。 To this end, in the present invention, in the resin kneading and plasticizing apparatus, a plurality of axially intermittent recesses are provided on the inner surface of the heating cylinder in the plasticizing and kneading zone of the heating cylinder, and single or single recesses are provided in the plasticizing and kneading zone of the screw. A dalmage portion having a plurality of dalmages was provided.
つぎに、図面に示した実施例によつて、本発明
を説明する。なお、本発明において、第1〜3図
に示す従来の装置と同じ部分は同一の付号で示
し、その説明は省略する。 Next, the present invention will be explained with reference to embodiments shown in the drawings. In the present invention, the same parts as in the conventional apparatus shown in FIGS. 1 to 3 are denoted by the same reference numbers, and the explanation thereof will be omitted.
第4〜7図は本発明の1実施例を示すものであ
る。第4図に示すように、加熱筒1の内面の可塑
化混練ゾーン5には、軸方向に所望の限定した長
さで断続させた複数個の凹部20を、千鳥状に配
置して設け、第5図に示すように、スクリユ7の
可塑化混練ゾーン5には、ダルメージ21を複数
個設けた、凹部20と、ダルメージ21部のダル
メージフライト22やフライト溝空間23の形
状、配置は、例えば、第6図の断面図と第7図の
展開図に示すようにし、フライト溝空間23と凹
部20の横断面形状は、例えば、単純な円弧状に
なるようにした。この場合のダルメージフライト
クリアランスは、例えば、スクリユフライトクリ
アランスと同じ寸法にした。 4 to 7 show one embodiment of the present invention. As shown in FIG. 4, the plasticization kneading zone 5 on the inner surface of the heating cylinder 1 is provided with a plurality of recesses 20 arranged in a staggered manner and intermittent at a desired limited length in the axial direction. As shown in FIG. 5, the plasticizing and kneading zone 5 of the screw 7 has a recess 20 provided with a plurality of dullages 21, and the shape and arrangement of the dullage flights 22 and flight groove spaces 23 in the dullage 21 portion are as follows. For example, as shown in the cross-sectional view of FIG. 6 and the developed view of FIG. 7, the cross-sectional shapes of the flight groove space 23 and the recess 20 are, for example, a simple circular arc shape. In this case, the dalmage flight clearance has the same dimensions as the screw flight clearance, for example.
第7図に示すように、ダルメージ21部のダル
メージフライト22が加熱筒1の凹部20位置に
来ればダルメージフライト22間の溝空間23の
材料は、スクリユ7と加熱筒1のスクリユ回転に
よる相対運動により、ダルメージフライト22を
乗越えて後方のダルメージフライト22間の溝空
間23へ移動する。しかし、前述の従来技術の方
法と異り、軸方向の加熱筒1内面の溝状の凹部2
0が連続的でなく断続千鳥配置であるため、後方
への漏洩流は限定され、可塑化能力の低下を防止
できる。又、加熱筒1の凹部20の軸方向の間隔
24により、安定して材料を推進する推進圧を維
持できる為、可塑化計量の不安定がなくなる。し
たがつて、混練や樹脂温度のバラツキも解消でき
る。一方、ダルメージフライト22は加熱筒1と
相対移動を回転方向及び軸方向においても行うた
め、ダルメージフライト22を材料が乗越えて、
加熱筒凹部20の空間を経て、後方のダルメージ
21の溝空間23へ移動する過程で切返し、重ね
合わせ等の混練作用は、どのダルメージ溝空間2
3の材料も一様に受け、優れた分散の機能は失わ
れない。すなわち、このように、本発明は可塑化
能力の低下を防ぎ、フイラーの切断破損を最小に
して、安定して計量すべきダルメージ21部の推
進圧を維持し、混練分散機能を十分維持するとい
う大きな効果を有する。 As shown in FIG. 7, when the dullage flights 22 of the dullage 21 come to the position of the recess 20 of the heating cylinder 1, the material in the groove space 23 between the dullmage flights 22 is removed by the screw rotation of the screw 7 and the heating cylinder 1. Due to the relative movement, it moves over the dalmage flights 22 and into the groove space 23 between the dalmage flights 22 at the rear. However, unlike the method of the prior art described above, the groove-shaped recess 2 on the inner surface of the heating cylinder 1 in the axial direction
Since the 0 is not continuous but is arranged in an intermittent staggered manner, leakage flow to the rear is limited and a decrease in plasticizing ability can be prevented. Furthermore, the axial spacing 24 between the recesses 20 of the heating cylinder 1 makes it possible to stably maintain the propulsion pressure that propels the material, thereby eliminating instability in plasticizing and metering. Therefore, variations in kneading and resin temperature can also be eliminated. On the other hand, since the Dalmage flight 22 moves relative to the heating cylinder 1 both in the rotational direction and the axial direction, the material can overcome the Dalmage flight 22,
In the process of moving through the space of the heating cylinder recess 20 to the groove space 23 of the rear dalmage 21, kneading operations such as turning and overlapping are performed in which dalmage groove space 2.
Material No. 3 was also uniformly received, and the excellent dispersion function was not lost. In other words, the present invention prevents the deterioration of the plasticizing ability, minimizes breakage of the filler, maintains the propelling pressure of the 21 parts of dalmage to be stably measured, and sufficiently maintains the kneading and dispersion function. It has a great effect.
更に、本発明のダルメージ21部を詳細に説明
すれば、第8図に示すように、ダルメージフライ
ト22と加熱筒1の内面25との間のダルメージ
フライトクリアランス26は材料を前方へ移送す
るに必要な推進圧を維持すべく必要なスクリユの
フライトクリアランスaであることは勿論である
が、フライトクリアランスの一部を、第8図に2
7および寸法bとして示すように拡げて、材料が
フライト22を乗越えてずり剪断作用を与えられ
るようシユアリングクリアランスとも言うことが
できる他のダルメージフライトクリアランス27
を設けると混練分散に大きい効果が得られる。こ
の場合、寸法aで示すダルメージフライトクリア
ランス26はスクリユフライトクリアランスと同
一にし、寸法bで示すダルメージフライトクリア
ランス27はスクリユフライトクリアランスaよ
りも大きくした。 Further, to explain the dullage 21 part of the present invention in detail, as shown in FIG. Of course, this is the flight clearance a of the screw necessary to maintain the necessary propulsion pressure, but a part of the flight clearance is shown in Figure 8.
7 and another dullage flight clearance 27 which can be expanded as shown as dimension b and may be referred to as a shearing clearance so that the material can overcome the flights 22 and be subjected to shear shearing action.
If provided, a large effect on kneading and dispersion can be obtained. In this case, the dullage flight clearance 26 indicated by the dimension a was made the same as the screw flight clearance, and the dullage flight clearance 27 indicated by the dimension b was made larger than the screw flight clearance a.
なお、このシユアリングクリアランスでもある
ダルメージフライトクリアランス27は、第9〜
11図に示すように、ダルメージ21部の入口側
クリアランb1を大きく、出口側クリアランスb2を
小さくすることが望ましい。つまり、樹脂の粘度
が高い領域では、強い剪断作用を与えないで、大
きく圧縮、変形、切返し、重ね合わせのような混
練作用を行わせることが望ましく、粘度が小さく
なつた領域では、比較的にクリアランスを小さく
して、粘度の低下した材料により良い分散作用を
与えることが望ましいためである。したがつて、
ダルメージ21部をこのようにすることもでき
る。 In addition, this shearing clearance, Dalmage Flight Clearance 27, is the 9th to
As shown in FIG. 11, it is desirable to make the entrance side clearance b 1 of the dalmage 21 section large and the exit side clearance b 2 small. In other words, in regions where the viscosity of the resin is high, it is desirable to perform large kneading actions such as compression, deformation, turning, and overlapping without applying strong shearing action, whereas in regions where the viscosity is low, it is desirable to perform kneading actions such as compression, deformation, turning, and overlapping. This is because it is desirable to reduce the clearance and give a better dispersion effect to the material whose viscosity has decreased. Therefore,
The 21st part of Dalmage can also be made like this.
また、第12図に示すダルメージ21部は、ダ
ルメージ30とダルメージ31から構成されてお
り、もし、各々単独に存在させて正規な回転方向
に回転させたならば、回転により材料を前方へ推
進するダルメージ30に対して、材料が逆送り効
果を有するダルメージ31を設けることもできる
が、その場合、ダルメージフライトクリアランス
26,27をスクリユフライトクリアランスaよ
りも大きくし、逆送り作用よりも剪断作用を重視
した方がよい。 Further, the dalmage 21 section shown in FIG. 12 is composed of a dalmage 30 and a dalmage 31, and if each of them exists independently and is rotated in the normal rotation direction, the rotation will propel the material forward. It is also possible to provide a dulbage 31 whose material has a reverse feeding effect with respect to the dullage 30, but in that case, the dullage flight clearances 26 and 27 are made larger than the screw flight clearance a, so that the shearing action is more effective than the reverse feeding action. It is better to focus on
更に、加熱筒1の内面の凹部20の他の実施例
を説明すると、第13〜15図に示すような円周
方向に長く、千鳥状に配した凹部20や、第16
〜18図に示すように円周方向に分割した複数の
凹部を軸方向に千鳥状に配置した凹部20を設け
ることができる。そして、このことにより、可塑
化混練部の推進圧力の低下を防止し、混練機能の
低下を防止し、可塑化能力の向上と可塑化の安定
に寄与することができる。 Furthermore, other embodiments of the recesses 20 on the inner surface of the heating cylinder 1 are described, such as recesses 20 that are long in the circumferential direction and arranged in a staggered manner as shown in FIGS.
As shown in Figures 1 to 18, it is possible to provide a recess 20 in which a plurality of recesses divided in the circumferential direction are arranged in a staggered manner in the axial direction. This can prevent the propulsion pressure of the plasticizing and kneading section from decreasing, preventing the kneading function from decreasing, and contributing to improving the plasticizing ability and stabilizing the plasticizing.
このように、本発明によれば、前述したよう
に、可塑化能力の低下を生じることなく、混練分
散にすぐれ、可塑化計量の安定したすぐれた可塑
化混練を確実容易に得ることができる。 As described above, according to the present invention, as described above, it is possible to reliably and easily obtain excellent plasticizing kneading with excellent kneading and dispersion and stable plasticizing measurement without causing a decrease in plasticizing ability.
第1〜3図は本発明に類した従来の装置の例を
示すもので、第1図は縦断面図、第2図は第1図
の−線断面図、第3図は展開図、第4〜7図
は本発明の第1実施例を示すもので、第4図は加
熱筒のみの縦断面図、第5図はスクリユと加熱筒
を示す縦断面図、第6図は第5図の−線断面
図、第7図は展開図、第8図は本発明の第2実施
例を示す加熱筒とダルメージ部の横断面図、第9
図は本発明の第3実施例を示すダルメージ部の正
面図、第10図は第9図の−線断面図、第1
1図は第9図のXI−XI線断面図、第12図は本発
明の第4実施例を示すダルメージ部の正面図、第
13図は本発明の第5実施例を示す加熱筒の縦断
面図、第14図および第15図はそれぞれ第13
図の−線断面図および−線断面
図、第16図は本発明の第6実施例を示す加熱筒
の縦断面図、第17図および第18図はそれぞれ
第16図の−線断面図および−
線断面図である。
1……加熱筒、2……材料供給口、3……ベン
ト孔、4……材料供給ゾーン、5……可塑化混練
ゾーン、6……溝、7……スクリユ、8……多条
ねじ、20……凹部、21,30,31……ダル
メージ、22……ダルメージフライト、23……
溝空間、26,27……ダルメージフライトクリ
アランス。
Figures 1 to 3 show examples of conventional devices similar to the present invention, where Figure 1 is a longitudinal sectional view, Figure 2 is a sectional view taken along the - line in Figure 1, and Figure 3 is a developed view. 4 to 7 show the first embodiment of the present invention. FIG. 4 is a vertical sectional view of only the heating cylinder, FIG. 5 is a vertical sectional view showing the screw and heating cylinder, and FIG. 6 is a vertical sectional view of the heating cylinder. FIG. 7 is a developed view, FIG. 8 is a cross-sectional view of the heating cylinder and dalmage portion showing the second embodiment of the present invention, and FIG.
The figure is a front view of the dalmage part showing the third embodiment of the present invention, FIG.
Fig. 1 is a sectional view taken along the line XI-XI in Fig. 9, Fig. 12 is a front view of the dalmage section showing the fourth embodiment of the present invention, and Fig. 13 is a longitudinal cross-section of the heating cylinder showing the fifth embodiment of the present invention. The front view, Figures 14 and 15 are respectively No. 13.
16 is a vertical sectional view of a heating cylinder showing a sixth embodiment of the present invention, and FIGS. 17 and 18 are a sectional view and a sectional view taken along a line in FIG. −
FIG. 1...Heating tube, 2...Material supply port, 3...Vent hole, 4...Material supply zone, 5...Plasticization and kneading zone, 6...Groove, 7...Screw, 8...Multi-thread screw , 20... recess, 21, 30, 31... dalmage, 22... dalmage flight, 23...
Groove space, 26, 27... Dalmage flight clearance.
Claims (1)
に摺動自在に設けたスクリユとからなり、加熱筒
内は材料供給口側より、材料供給ゾーン、可塑化
混練ゾーン、脱気ゾーン、計量ゾーンが順次形成
されている樹脂の混練可塑化装置において、前記
加熱筒の可塑化混練ゾーンに、軸方向に断続した
凹部を加熱筒内面に複数個設け、スクリユの可塑
化混練ゾーンに、単一もしくは複数個のダルメー
ジを有するダルメージ部を設けた樹脂の混練可塑
化装置。 2 スクリユの可塑化混練ゾーンのダルメージ部
のダルメージフライトクリアランスを、ダルメー
ジフライトの少くとも一つ以上はスクリユフライ
トクリアランス以上に大きくし、ダルメージフラ
イトクリアランス部で材料にずり剪断作用を与え
るようにした特許請求の範囲第1項記載の樹脂の
混練可塑化装置。 3 スクリユの可塑化混練ゾーンのダルメージ部
のダルメージフライトのクリアランスを、ダルメ
ージフライトの少くとも一つ以上はスクリユフラ
イトクリアランスより大きくし、ダルメージ部上
流のダルメージフライトクリアランスを下流のダ
ルメージフライトクリアランスより大きくした特
許請求の範囲第1項記載の樹脂の混練可塑化装
置。 4 ダルメージ部の少くとも一つ以上のダルメー
ジが材料を逆推進させるようにダルメージフライ
トを設け、該ダルメージフライトクリアランスを
スクリユフライトクリアランスより大きくした特
許請求の範囲第1項記載の樹脂の混練可塑化装
置。[Claims] 1. Consists of a heating cylinder and a screw rotatably and slidably provided in the heating cylinder in the heating cylinder, and the inside of the heating cylinder is arranged from the material supply port side to the material supply zone, plasticization kneading zone, In a resin kneading and plasticizing apparatus in which a zone, a degassing zone, and a metering zone are sequentially formed, a plurality of axially interrupted recesses are provided on the inner surface of the heating cylinder in the plasticizing and kneading zone of the heating cylinder, and the plasticization of the screw A resin kneading and plasticizing device in which a dullage section having a single or plural dullages is provided in a plasticizing and kneading zone. 2 The dullage flight clearance of the dullage part of the plasticization kneading zone of the screw is made larger than the screw flight clearance for at least one of the dullage flights, so that shearing action is applied to the material in the dullage flight clearance part. A resin kneading and plasticizing apparatus according to claim 1. 3. Make the clearance of the Dalmage flight in the Dalmage part of the plasticization kneading zone of the Skrill larger than the Scrillage flight clearance of at least one Dalmage flight, and make the Dalmage flight clearance upstream of the Dalmage part equal to the Dalmage flight clearance of the downstream Dalmage flight. The resin kneading and plasticizing apparatus according to claim 1, wherein the clearance is larger than the clearance. 4. The kneading of the resin according to claim 1, wherein a dullage flight is provided so that at least one dullage in the dullage portion propels the material backward, and the dullage flight clearance is larger than the screw flight clearance. Plasticizing equipment.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP58043068A JPS59169826A (en) | 1983-03-17 | 1983-03-17 | Resin kneading and plasticizing equipment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP58043068A JPS59169826A (en) | 1983-03-17 | 1983-03-17 | Resin kneading and plasticizing equipment |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS59169826A JPS59169826A (en) | 1984-09-25 |
| JPH0337495B2 true JPH0337495B2 (en) | 1991-06-05 |
Family
ID=12653533
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP58043068A Granted JPS59169826A (en) | 1983-03-17 | 1983-03-17 | Resin kneading and plasticizing equipment |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS59169826A (en) |
Families Citing this family (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS6241015A (en) * | 1985-08-16 | 1987-02-23 | Idemitsu Petrochem Co Ltd | Screw for molding thermoplastic resin |
| JPS6241016A (en) * | 1985-08-16 | 1987-02-23 | Idemitsu Petrochem Co Ltd | Screw for molding thermoplastic resin |
| JPS62146611A (en) * | 1985-12-20 | 1987-06-30 | Idemitsu Petrochem Co Ltd | Manufacture of crystalline thermoplastic resin sheet |
| JPS648015A (en) * | 1987-07-01 | 1989-01-12 | Kishimoto Sangyo Co | Vent type injection molding machine for composite plastic |
| US5332314A (en) * | 1992-07-06 | 1994-07-26 | Paul Geyer | Extrusion apparatus with a backfeed extruder for mixing and extruding of thermo-plastic and thermo-setting materials |
-
1983
- 1983-03-17 JP JP58043068A patent/JPS59169826A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS59169826A (en) | 1984-09-25 |
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