JP5142390B2 - Plasticizing apparatus and plasticizing method - Google Patents

Plasticizing apparatus and plasticizing method Download PDF

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JP5142390B2
JP5142390B2 JP2008241008A JP2008241008A JP5142390B2 JP 5142390 B2 JP5142390 B2 JP 5142390B2 JP 2008241008 A JP2008241008 A JP 2008241008A JP 2008241008 A JP2008241008 A JP 2008241008A JP 5142390 B2 JP5142390 B2 JP 5142390B2
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screw
main flight
plasticizing
zone
flight
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JP2010069771A (en
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一也 阿南
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株式会社名機製作所
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    • 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
    • B29C48/88Thermal treatment of the stream of extruded material, e.g. cooling
    • B29C48/918Thermal treatment of the stream of extruded material, e.g. cooling characterized by differential heating or cooling
    • B29C48/9185Thermal treatment of the stream of extruded material, e.g. cooling characterized by differential heating or cooling in the direction of the stream of the material
    • 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
    • B29C48/375Plasticisers, homogenisers or feeders comprising two or more stages
    • B29C48/39Plasticisers, homogenisers or feeders comprising two or more stages a first extruder feeding the melt into an intermediate location of a second extruder
    • 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
    • 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
    • B29C48/92Measuring, controlling or regulating
    • 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
    • B29C2948/00Indexing scheme relating to extrusion moulding
    • B29C2948/92Measuring, controlling or regulating
    • B29C2948/92504Controlled parameter
    • B29C2948/9258Velocity
    • B29C2948/9259Angular velocity
    • 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
    • B29C2948/00Indexing scheme relating to extrusion moulding
    • B29C2948/92Measuring, controlling or regulating
    • B29C2948/92819Location or phase of control
    • B29C2948/92857Extrusion unit
    • B29C2948/92876Feeding, melting, plasticising or pumping zones, e.g. the melt itself
    • B29C2948/92885Screw or gear

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  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (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

本発明は、加熱筒内の排気を良好にする可塑化装置および可塑化方法に関するものである。 The present invention relates to a plasticizing apparatus and a plasticizing method for improving exhaust in a heating cylinder.

シリンダ(加熱筒)内を真空ポンプにより排気した状態で主フライトと副フライトを備えたスクリュを回転して可塑化し、可塑化中に発生するガスを排気する技術は、特許文献1に開示されている。しかしながら、特許文献1における副フライト部で発生したガスの排気状況は、本願の図4に示すように、良好ではない。すなわち、副フライトを乗り越えて主フライトの前面に堆積した溶融材料から効果的に発生したガスは、副フライトを乗り越えて主フライトの後面側に流入した後、半溶融材料や未溶融の原料ペレットの間隙を経由して流動せねばならず、極めて大きな流動抵抗が生じるのである。 A technique for rotating and plasticizing a screw provided with a main flight and a subflight in a state where the inside of a cylinder (heating cylinder) is exhausted by a vacuum pump and exhausting a gas generated during plasticization is disclosed in Patent Document 1. Yes. However, as shown in FIG. 4 of the present application, the exhaust state of the gas generated in the subflight portion in Patent Document 1 is not good. That is, the gas generated effectively from the molten material deposited on the front of the main flight over the subflight flows over the subflight and flows into the rear side of the main flight, and then the semi-molten material and unmelted raw material pellets. It must flow through the gap, resulting in a very large flow resistance.

一方、特許文献2には、シリンダ内に存する空気、成形材料から発生したガス等の気体を除去するため、スクリュの螺旋状の山部の複数箇所に、軸線方向に貫通する溝または穴を設けることが開示されている。しかしながら、特許文献2の技術によれば、前記溝または穴には成形材料が入り込んで排気を妨げる虞があり、それを回避するため溝または穴を大きくした場合には、可塑化能力の低下が懸念される。 On the other hand, in Patent Document 2, in order to remove gas such as air generated in the cylinder and gas generated from the molding material, grooves or holes penetrating in the axial direction are provided at a plurality of locations on the spiral crest of the screw. It is disclosed. However, according to the technique of Patent Document 2, there is a possibility that molding material may enter the groove or hole and hinder exhaust, and if the groove or hole is enlarged to avoid this, the plasticizing ability is reduced. Concerned.

実公平3−53867号公報Japanese Utility Model Publication No. 3-53867 特開平8−142143号公報JP-A-8-142143

本発明は、上記した問題を解決すべくなされたものであって、副フライトを備えたスクリュによる可塑化装置におけるガスの排気を効果的に向上させる可塑化装置および可塑化方法を提供することを目的とする。 The present invention has been made to solve the above-described problems, and provides a plasticizing apparatus and a plasticizing method for effectively improving gas exhaustion in a plasticizing apparatus using a screw provided with a subflight. Objective.

上記課題を解決するため、請求項1に記載の発明は、フィードゾーン、コンプレッションゾーン及びメタリングゾーンを有する原料可塑化用のスクリュを備え、加熱筒の内部を強制排気可能に構成した可塑化装置であって、前記フィードゾーン、コンプレッションゾーン及びメタリングゾーンに連続して螺旋状に形成され前記スクリュを嵌挿する加熱筒の内孔の内径より僅か小さい外径を有する主フライトと、前記主フライトのフィードゾーンとメタリングゾーンとの間の任意の区間における前記主フライトの前面と後面との間に一又は複数形成され前記主フライトの外径より小さい外径を有する副フライトと、前記副フライトが接続される前記主フライトの前面部分から前方近傍の主フライトのみに主フライトピッチ間隔の半分までの幅に設けた切り欠きからなる通気部とが設けられたスクリュを備えたことをその要旨としている。 In order to solve the above-mentioned problem, the invention described in claim 1 is a plasticizer comprising a screw for plasticizing a raw material having a feed zone, a compression zone, and a metering zone, and configured to allow forced exhaust of the inside of the heating cylinder. A main flight having an outer diameter slightly smaller than an inner diameter of an inner hole of a heating cylinder formed in a spiral shape continuously to the feed zone, the compression zone and the metering zone, and inserting the screw; A subflight having an outer diameter smaller than the outer diameter of the main flight, wherein one or a plurality of subflights are formed between a front surface and a rear surface of the main flight in an arbitrary section between the feed zone and the metering zone; To the width of the main flight pitch interval from the front portion of the main flight to the main flight near the front That the ventilation unit consisting outs Kita cut is provided with a screw provided is the gist thereof.

これによれば、極めて良好にガスの排気を行うことができる。 According to this, gas can be exhausted extremely well.

請求項2に記載の発明は、請求項1に記載のスクリュを備えた可塑化装置であって、前記加熱筒へ供給する原料を制限制御する原料調節手段を備えたことをその要旨としている。 The gist of the invention described in claim 2 is the plasticizing apparatus provided with the screw according to claim 1, and is provided with a raw material adjusting means for restricting and controlling the raw material supplied to the heating cylinder.

これによれば、ガスの排出をより効果的に行うことができる。 According to this, gas can be discharged more effectively.

請求項3に記載の発明は、請求項1または請求項2に記載の可塑化装置を用いた可塑化方法であって、前記可塑化装置で設定可能な最大回転速度の50%以上の回転速度で前記スクリュを回転駆動するとともに、スクリュ背圧力を溶融材料の圧力において0〜5MPaの範囲で制御することをその要旨としている。 Invention of Claim 3 is a plasticizing method using the plasticizing apparatus of Claim 1 or Claim 2 , Comprising: The rotational speed of 50% or more of the maximum rotational speed which can be set with the said plasticizing apparatus The gist is to rotate the screw and control the screw back pressure in the range of 0 to 5 MPa in the pressure of the molten material.

これによれば、溶融材料からの脱気が極めて容易に行われる。 According to this, degassing from the molten material is performed very easily.

本発明は、フィードゾーン、コンプレッションゾーン及びメタリングゾーンを有する原料可塑化用のスクリュを備え、加熱筒の内部を強制排気可能に構成した可塑化装置が、前記フィードゾーン、コンプレッションゾーン及びメタリングゾーンに連続して螺旋状に形成され前記スクリュを嵌挿する加熱筒の内孔の内径より僅か小さい外径を有する主フライトと、前記主フライトのフィードゾーンとメタリングゾーンとの間の任意の区間における前記主フライトの前面と後面との間に一又は複数形成され前記主フライトの外径より小さい外径を有する副フライトと、前記副フライトが接続される前記主フライトの前面部分から前方近傍の主フライトのみに主フライトピッチ間隔の半分までの幅に設けた切り欠きからなる通気部とが設けられたスクリュを備えるので、極めて良好にガスの排気を行うことができる。 The present invention provides a plasticizing apparatus comprising a feed plasticizing screw having a feed zone, a compression zone, and a metering zone, and configured to be capable of forcibly exhausting the inside of the heating cylinder, the feed zone, the compression zone, and the metering zone. A main flight having an outer diameter slightly smaller than an inner diameter of an inner hole of a heating cylinder that is formed in a spiral shape and is inserted into the screw, and an arbitrary section between a feed zone and a metering zone of the main flight A subflight having one or more formed between the front surface and the rear surface of the main flight and having an outer diameter smaller than the outer diameter of the main flight, and a front flight portion from the front portion of the main flight to which the subflight is connected. Only main flights are provided with vents consisting of notches with a width of up to half of the main flight pitch interval. Since comprises Ryu, it can be carried out very well exhaust gas.

図面に基づいて、本発明の実施の形態を詳細に説明する。図1は、本発明のスクリュを備えた可塑化装置の縦断面図である。図2は、本発明の可塑化装置に用いられるスクリュにおけるフライトの展開図である。図3は、本発明の可塑化装置に用いられる他のスクリュにおけるフライトの展開図である。図4は、従来のスクリュにおけるフライトの展開図である。 Embodiments of the present invention will be described in detail with reference to the drawings. FIG. 1 is a longitudinal sectional view of a plasticizing apparatus provided with the screw of the present invention. FIG. 2 is a development view of a flight in a screw used in the plasticizing apparatus of the present invention. FIG. 3 is a developed view of a flight in another screw used in the plasticizing apparatus of the present invention. FIG. 4 is a development view of a flight in a conventional screw.

可塑化装置1は、スクリュヘッド6とリングバルブ7でなる逆止弁を先端に備えたスクリュ2と、スクリュ2を回転往復動可能に嵌挿し先端面にノズル9を外周面にバンドヒータ10を備えた加熱筒8と、加熱筒8後部上面の貫通穴に連通する原料落下口12を有し加熱筒8の後部を固着するハウジング11と、ハウジング11の上面に原料落下口12へ連通するように固着され原料調節筒13とフィードスクリュ14でなる原料調節手段15と、原料落下口12の上方の原料調節筒13上面に設けた貫通穴に接続された真空ポンプ19と、原料調節筒13の上面に立設した原料供給筒16とからなる。スクリュ2は、ハウジング11の延長部に連結した図示しない駆動手段を図示しない制御装置で設定した設定値に基づいて回転又は前後進するように制御される。原料供給筒16は、交互に開閉する二のシャッタ17,18により上下に三の部屋を画設して、原料調節手段15へ気密を保持しつつ所定量の原料Mを供給する。シャッタ17,18の摺動部及びフィードスクリュ14とスクリュ2の駆動軸部分には、摺動又は回転しても気密が保持できるようなパッキングが設けられている。また、真空ポンプ19は、原料調節筒13上面に設けた貫通穴に接続するよう例示したが、原料落下口12に設けた貫通穴か、加熱筒8の後端部か、スクリュ2が最後退したときの通気部5に対向する加熱筒8の中間部より後部に設けた貫通穴に接続してもよい。なお、可塑化装置1は、射出成形機のものとして例示したが、押出し機であってもよい。 The plasticizing apparatus 1 includes a screw 2 having a check valve composed of a screw head 6 and a ring valve 7 at the tip, and a screw 2 that is fitted to the screw 2 so as to be able to rotate and reciprocate. A heating cylinder 8 provided, a housing 11 having a raw material dropping port 12 communicating with a through-hole on the upper surface of the rear portion of the heating cylinder 8, and a raw material dropping port 12 on the upper surface of the housing 11 so as to communicate with the raw material dropping port 12 A raw material adjusting means 15 comprising a raw material adjusting cylinder 13 and a feed screw 14, a vacuum pump 19 connected to a through hole provided on the upper surface of the raw material adjusting cylinder 13 above the raw material dropping port 12, It consists of a raw material supply cylinder 16 erected on the upper surface. The screw 2 is controlled so that a driving means (not shown) connected to an extension of the housing 11 rotates or moves forward and backward based on a set value set by a control device (not shown). The raw material supply cylinder 16 is provided with three chambers up and down by two shutters 17 and 18 that are alternately opened and closed, and supplies a predetermined amount of the raw material M to the raw material adjusting means 15 while maintaining airtightness. The sliding portions of the shutters 17 and 18 and the drive shaft portions of the feed screw 14 and the screw 2 are provided with packing that can maintain airtightness even when sliding or rotating. In addition, the vacuum pump 19 is illustrated as being connected to the through hole provided on the upper surface of the raw material adjusting cylinder 13, but the through hole provided in the raw material dropping port 12, the rear end of the heating cylinder 8, or the screw 2 is retracted last. You may connect to the through-hole provided in the rear part from the intermediate part of the heating cylinder 8 which opposes the ventilation | gas_flowing part 5 at that time. In addition, although the plasticizing apparatus 1 was illustrated as that of an injection molding machine, it may be an extruder.

スクリュ2は、基部が小径で先端部が大径であって中間部は小径と大径を滑らかに接続する円錐台状である軸部22としての丸棒の外周に、主フライト3としての壁状突出体が基部から先端部まで連続して螺旋状に形成されたものである。この主フライト3の外径は、加熱筒8の内孔の内径より僅か小さい。そして、スクリュ2は、前記基部の小径区間をフィードゾーンZFとし、前記中間部をコンプレッションゾーンZCとし、先端部の大径区間をメタリングゾーンZMとしてその軸方向に区画されている。 The screw 2 has a wall as a main flight 3 on the outer periphery of a round bar as a shaft portion 22 having a small diameter at the base and a large diameter at the tip, and a middle portion having a truncated cone shape that smoothly connects the small diameter and the large diameter. The protrusions are formed in a continuous spiral from the base to the tip. The outer diameter of the main flight 3 is slightly smaller than the inner diameter of the inner hole of the heating cylinder 8. The screw 2 is partitioned in the axial direction with the small diameter section of the base portion as a feed zone ZF, the intermediate portion as a compression zone ZC, and the large diameter section of the tip portion as a metering zone ZM.

スクリュ2は、主フライト3のフィードゾーンZFとメタリングゾーンZMとの間の任意の区間における主フライト3の前面20と後面21との間に一又は複数形成され主フライト3の外径より小さい外径の副フライト4を有する。すなわち、図1に示す実施態様では、副フライト4は、フィードゾーンZFとコンプレッションゾーンZCとの境界部分の主フライト3の前面20に接続され、そこから主フライト3の前方3ピッチ目にあたるコンプレッションゾーンZC中間の主フライト3の後面21まで連続して設けられている。このように、副フライト4は一のみ設けてもよいが、主フライト3のフィードゾーンZFとメタリングゾーンZMとの間に、複数設けてもよい。また、複数の副フライトは、同一のピッチ間隔を有するものであっても、相互に異なるピッチ間隔を有するものであってもよい。主フライト3と副フライト4が分岐する部分の前方における三角形の部分24は、軸部22の外径に向けてなだらかに低くなっている。 One or a plurality of screws 2 are formed between the front surface 20 and the rear surface 21 of the main flight 3 in an arbitrary section between the feed zone ZF and the metering zone ZM of the main flight 3 and are smaller than the outer diameter of the main flight 3. It has a secondary flight 4 with an outer diameter. That is, in the embodiment shown in FIG. 1, the secondary flight 4 is connected to the front surface 20 of the main flight 3 at the boundary between the feed zone ZF and the compression zone ZC, and the compression zone corresponding to the third forward pitch of the main flight 3 therefrom. It is provided continuously up to the rear surface 21 of the main flight 3 in the middle of the ZC. Thus, although only one subflight 4 may be provided, a plurality of subflights 4 may be provided between the feed zone ZF and the metering zone ZM of the main flight 3. Further, the plurality of subflights may have the same pitch interval or may have different pitch intervals. A triangular portion 24 in front of a portion where the main flight 3 and the sub flight 4 are branched is gradually lowered toward the outer diameter of the shaft portion 22.

主フライト3に対して副フライトが接続される主フライトの前面部分20aから前方近傍の主フライト3には、通気部5が設けられている。通気部5は、主フライト3をスクリュ2の軸線に平行な方向又はその近傍で貫通する切り欠き又は貫通穴であることが好ましい。通気部5が切り欠きであるときの具体的数値は、可塑化装置1の可塑化能力の大きさすなわちスクリュ2サイズに応じて変化するので、記載は困難である。しかしながら、切り欠きの深さは軸部22の面まで達し、切り欠きの幅は主フライト3のピッチ間隔の半分に相当する間隔までであることが効果的である。特には、切り欠きの幅の広いことが、フィードゾーンZFにプラスチックペレット等からなる原料Mを充満させて副フライト4の存在する主フライト3の前面20部を清掃するときに、原料M又は半溶融材料MHの流入を容易にする点において効果的である。なお前記三角形の部分24に隣接する主フライト3は、スクリュ加工上の理由から通気部5を設けない場合が多い。 A ventilation portion 5 is provided in the main flight 3 near the front from the front portion 20a of the main flight to which the sub flight is connected to the main flight 3. The ventilation portion 5 is preferably a notch or a through hole that penetrates the main flight 3 in a direction parallel to the axis of the screw 2 or in the vicinity thereof. Since the specific numerical value when the ventilation part 5 is a notch changes according to the magnitude | size of the plasticizing capability of the plasticizing apparatus 1, ie, the screw 2 size, description is difficult. However, it is effective that the depth of the notch reaches the surface of the shaft portion 22 and the width of the notch is up to an interval corresponding to half the pitch interval of the main flight 3. In particular, when the notch has a wide width, when the feed zone ZF is filled with the raw material M made of plastic pellets or the like and the front portion 20 of the main flight 3 where the sub-flight 4 is present is cleaned, the raw material M or half This is effective in facilitating the inflow of the molten material MH. In many cases, the main flight 3 adjacent to the triangular portion 24 is not provided with the ventilation portion 5 for reasons of screw processing.

次に、図2〜図4に基づいてスクリュ2における可塑化の作用とその効果について詳細に説明する。図2〜図4は、スクリュ2の主フライト3,3b,3cと、その前面20と後面21の間に接続された副フライト4,4a,4bとの関係を示して可塑化状況を解り易くするために展開したものである。原料Mは図の右側からスクリュ2の回転に伴って搬送され、副フライト4,4a,4bで半溶融材料MH又は一部が溶融材料MMの状態となり、副フライト4,4a,4bを乗り越えて主フライト3,3b,3cの前面20側に堆積する。 Next, based on FIGS. 2-4, the plasticization effect | action in the screw 2 and its effect are demonstrated in detail. 2 to 4 show the relationship between the main flights 3, 3b, 3c of the screw 2 and the sub-flights 4, 4a, 4b connected between the front surface 20 and the rear surface 21 so that the plasticization state can be easily understood. It is developed to do. The raw material M is conveyed with the rotation of the screw 2 from the right side of the figure, and the sub-flights 4, 4a, 4b are in the state of a semi-molten material MH or a part of the molten material MM and get over the sub-flights 4, 4a, 4b. It accumulates on the front surface 20 side of the main flights 3, 3b, 3c.

そして、そのとき発生したガスG(水分も含み以下同じとする。)は、図4に示す従来の場合では、副フライト4bを乗り越えて主フライト3cの後面21側に流入した後、半溶融材料MHや未溶融の原料Mペレットの間隙を経由して流動するため、極めて大きな抵抗が生じ、容易に排気されないのである。 Then, in the conventional case shown in FIG. 4, the gas G generated at that time (including moisture hereinafter) gets over the subflight 4b and flows into the rear surface 21 side of the main flight 3c, and then the semi-molten material. Since it flows through the gaps between MH and unmelted raw material M pellets, an extremely large resistance is generated and it is not easily exhausted.

それに対し、図2に示す本発明の場合には、主フライト3前面20の溶融材料MMから放出したガスGは、副フライト4の主フライト3前面20と対向する面に形成された空間を流動して通気部5から、通気部5が設けられた主フライト3の後面21側に進入し、さらに、主フライト3の後面側に形成された螺旋状の空間を通過して加熱筒8内から大気中へ放出される。このとき、加熱筒8の後部や原料落下口12あるいは原料調節手段15に設けた貫通穴からガスGを自然放出させて排気してもよいが、本実施の形態に示すように、真空ポンプ19で真空吸引して強制的に排気すると極めて効果的にガスGの除去を行うことができる。また、原料調節手段15を設けて、原料落下口12に原料Mが充満しないようにフィードスクリュ14の回転速度を制御し、原料Mの供給量を制限制御する。これにより、フィードゾーンZFにおける原料Mの搬送量が減少して原料Mの存在しない螺旋状の空間が増加するとともに、副フライト4の主フライト3前面20と対向する面に形成された空間も増加しガスGの流通・通過が極めて容易になる。 On the other hand, in the case of the present invention shown in FIG. 2, the gas G released from the molten material MM on the front surface 20 of the main flight 3 flows in the space formed on the surface of the sub flight 4 facing the front surface 20 of the main flight 3. Then, the air enters the rear surface 21 side of the main flight 3 provided with the air ventilation portion 5 from the ventilation portion 5, and further passes through the spiral space formed on the rear surface side of the main flight 3 from the inside of the heating cylinder 8. Released into the atmosphere. At this time, the gas G may be naturally discharged from the rear portion of the heating cylinder 8, the raw material dropping port 12, or the through hole provided in the raw material adjusting means 15, and exhausted. However, as shown in the present embodiment, the vacuum pump 19 The gas G can be removed very effectively by vacuum suction and forced exhaust. Moreover, the raw material adjustment means 15 is provided, the rotational speed of the feed screw 14 is controlled so that the raw material M does not fill the raw material dropping port 12, and the supply amount of the raw material M is limited. As a result, the conveyance amount of the raw material M in the feed zone ZF decreases, and the spiral space where the raw material M does not exist increases, and the space formed on the surface facing the front surface 20 of the main flight 3 of the sub flight 4 also increases. However, the distribution and passage of the gas G is extremely easy.

また、図3に示す本発明の他の実施の形態では、前記主フライトにおける前記副フライト4aの後面23に対向する区間である小径部3aの外径は、前記主フライトにおける前記区間以外の区間の主フライト3b(フィードゾーンやメタリングゾーンの全部または過半の部分)の外径より小さく形成されている。したがって、主フライトの小径部3aの外径と副フライト4aの外径が同一の場合もあるから、前記小径部3aは、副フライト4aの外径以上の場合が含まれる。なお前記主フライトの小径部3aにより通気部を構成することにより、一箇所のみに主フライトの高さの低い部分を設けないようにしてもよい。なお前記主フライトの小径部3aは、過半の部分で副フライト4aと対向していればよく、副フライト4aより同一長さか、または副フライト4aよりも長くても短くてもよい。 Further, in another embodiment of the present invention shown in FIG. 3, the outer diameter of the small diameter portion 3a which is a section facing the rear surface 23 of the sub flight 4a in the main flight is a section other than the section in the main flight. Is formed smaller than the outer diameter of the main flight 3b (all or a majority of the feed zone and metering zone). Accordingly, since the outer diameter of the small-diameter portion 3a of the main flight may be the same as the outer diameter of the subflight 4a, the small-diameter portion 3a includes a case where the outer diameter of the subflight 4a is equal to or greater. In addition, you may make it not provide the part with the low height of a main flight only in one place by comprising a ventilation part by the small diameter part 3a of the said main flight. The small diameter portion 3a of the main flight only needs to be opposed to the sub flight 4a in the majority, and may be the same length as the sub flight 4a or longer or shorter than the sub flight 4a.

このように構成することにより、ガスGの排気は通気部5から容易に行えるとともに、副フライト4aにおける主フライトの小径部3aと対向する面で溶融材料MMが生成されるようなときであっても、排気が可能となるため可塑化能力の向上が図れる。なお、この図3の実施の形態の場合でも、真空ポンプ19と原料調節手段15を設ける効果は、上記した図2の実施の形態の場合と同様である。 With this configuration, the gas G can be easily exhausted from the ventilation portion 5 and the molten material MM is generated on the surface of the sub flight 4a facing the small diameter portion 3a of the main flight. However, since the exhaust can be performed, the plasticizing ability can be improved. In the case of the embodiment of FIG. 3, the effect of providing the vacuum pump 19 and the raw material adjusting means 15 is the same as that of the above-described embodiment of FIG.

原料Mを可塑化するため、スクリュ2を回転駆動制御するとき、上記のように脱気・排気された溶融材料MMは、メタリングゾーンZMから逆止弁を経由して加熱筒8の内孔前部に押し出され貯留される。そして、貯留された溶融材料MMの圧力によりスクリュ2は後退方向の力を受けて後退する。その後退力を駆動手段で制御することにより溶融材料MMの圧力すなわちスクリュ背圧力が制御されるのである。スクリュ背圧力は、その値が高ければ溶融材料MMの混練が良好となる反面、溶融材料MMからのガスGの放出を阻害させる。そのため、本発明の可塑化装置1で溶融材料MMからの良好な脱気を目的に可塑化を行うにあたり、発明者が鋭意試験・研究した結果、スクリュ背圧力が溶融材料MMの圧力で0〜5MPaの範囲であることが好ましいことを見出したのである。 When the screw 2 is rotationally driven to plasticize the raw material M, the molten material MM degassed and exhausted as described above is passed through the inner hole of the heating cylinder 8 from the metering zone ZM via the check valve. It is pushed out and stored in the front. Then, the screw 2 moves backward by receiving a force in the backward direction due to the pressure of the stored molten material MM. By controlling the retreating force by the driving means, the pressure of the molten material MM, that is, the screw back pressure is controlled. If the value of the screw back pressure is high, the kneading of the molten material MM becomes good, but the release of the gas G from the molten material MM is hindered. Therefore, as a result of inventor's diligent test and research in performing plasticization for the purpose of good degassing from the molten material MM in the plasticizing apparatus 1 of the present invention, the screw back pressure is 0 to the pressure of the molten material MM. It has been found that the range of 5 MPa is preferable.

また、可塑化中のスクリュ2の回転速度は、駆動手段の出力容量に基づいて必然的に決定された最大回転速度までの任意の値が制御装置で設定されて制御される。そして、スクリュ2の最大回転速度は可塑化装置1やスクリュ2のサイズ等に応じて変化する。したがって、溶融材料MMからの脱気を良好とするに最適なスクリュ2回転速度を絶対値で表現することは困難である。しかしながら、少なくとも、可塑化装置1で設定可能な最大回転速度の50%以上の回転速度でスクリュ2を回転駆動すると、溶融材料MMからの脱気を良好としつつ好ましい可塑化能力が得られることを見出した。このようにスクリュ回転速度を比較的高速に制御することにより、スクリュ2のフライトと溶融材料MM等との間でスクリュ2の回転に伴って生ずる螺子効果に基づくスクリュ2後退力が増大してスクリュ背圧力をより低下させるという相乗効果が得られる。 In addition, the rotational speed of the screw 2 during plasticization is controlled by setting an arbitrary value up to the maximum rotational speed inevitably determined based on the output capacity of the driving means by the control device. And the maximum rotational speed of the screw 2 changes according to the size etc. of the plasticizer 1 or the screw 2. Therefore, it is difficult to express the screw 2 rotation speed optimum for degassing the molten material MM as an absolute value. However, when the screw 2 is rotationally driven at least at a rotational speed of 50% or more of the maximum rotational speed that can be set by the plasticizing apparatus 1, it is possible to obtain a preferable plasticizing ability while improving degassing from the molten material MM. I found it. By controlling the screw rotation speed at a relatively high speed in this way, the screw 2 retracting force based on the screw effect caused by the rotation of the screw 2 between the flight of the screw 2 and the molten material MM or the like is increased and the screw is rotated. A synergistic effect of lowering the back pressure is obtained.

なお、本発明は、当業者の知識に基づいて様々な変更、修正、改良等を加えた態様において実施され得るものを含む。また、前記変更等を加えた実施態様が、本発明の趣旨を逸脱しない限りいずれも本発明の範囲内に含まれるものであることは言うまでもない。 In addition, this invention includes what can be implemented in the aspect which added various change, correction, improvement, etc. based on the knowledge of those skilled in the art. Further, it goes without saying that any of the embodiments to which the above-mentioned changes are added is included in the scope of the present invention without departing from the gist of the present invention.

本発明のスクリュを備えた可塑化装置の縦断面図である。It is a longitudinal cross-sectional view of the plasticizing apparatus provided with the screw of this invention. 本発明の可塑化装置に用いられるスクリュにおけるフライトの展開図である。It is an expanded view of the flight in the screw used for the plasticizing apparatus of this invention. 本発明の可塑化装置に用いられる他のスクリュにおけるフライトの展開図である。It is an expanded view of the flight in the other screw used for the plasticizing apparatus of this invention. 従来のスクリュにおけるフライトの展開図である。It is an expanded view of the flight in the conventional screw.

1 可塑化装置
2 スクリュ
3,3b,3c 主フライト
3a 小径部
4,4a,4b 副フライト
5 通気部
6 スクリュヘッド
7 リングバルブ
8 加熱筒
9 ノズル
10 バンドヒータ
11 ハウジング
12 原料落下口
13 原料調節筒
14 フィードスクリュ
15 原料調節手段
16 原料供給筒
17,18 シャッタ
19 真空ポンプ
20 前面
20a 副フライトが接続される主フライトの前面部分
21,22 後面
22 軸部
23 後面
24 三角形の部分
G ガス
M 原料
MH 半溶融材料
MM 溶融材料
ZF フィードゾーン
ZC コンプレッションゾーン
ZM メタリングゾーン
DESCRIPTION OF SYMBOLS 1 Plasticizer 2 Screw 3, 3b, 3c Main flight 3a Small diameter part 4, 4a, 4b Subflight 5 Ventilation part 6 Screw head 7 Ring valve 8 Heating cylinder 9 Nozzle 10 Band heater 11 Housing 12 Raw material drop port 13 Raw material adjustment cylinder 14 Feed screw 15 Raw material adjusting means 16 Raw material supply cylinders 17 and 18 Shutter 19 Vacuum pump 20 Front surface 20a Front portion 21 and 22 of main flight to which the secondary flight is connected Rear surface 22 Shaft portion 23 Rear surface 24 Triangular portion G Gas M Raw material MH Semi-molten material MM Molten material ZF Feed zone ZC Compression zone ZM Metalling zone

Claims (3)

フィードゾーン、コンプレッションゾーン及びメタリングゾーンを有する原料可塑化用のスクリュを備え、加熱筒の内部を強制排気可能に構成した可塑化装置であって、
前記フィードゾーン、コンプレッションゾーン及びメタリングゾーンに連続して螺旋状に形成され前記スクリュを嵌挿する加熱筒の内孔の内径より僅か小さい外径を有する主フライトと、前記主フライトのフィードゾーンとメタリングゾーンとの間の任意の区間における前記主フライトの前面と後面との間に一又は複数形成され前記主フライトの外径より小さい外径を有する副フライトと、前記副フライトが接続される前記主フライトの前面部分から前方近傍の主フライトのみに主フライトピッチ間隔の半分までの幅に設けた切り欠きからなる通気部とが設けられたスクリュを備えたことを特徴とする可塑化装置。
A plasticizing device comprising a feed plasticizing screw having a feed zone, a compression zone and a metering zone, and configured to allow forced exhaust of the inside of the heating cylinder,
A main flight having an outer diameter slightly smaller than an inner diameter of an inner hole of a heating cylinder formed in a spiral shape continuously to the feed zone, the compression zone, and the metering zone, and the feed zone of the main flight; The subflight is connected to one or more subflights having an outer diameter smaller than the outer diameter of the main flight formed between the front surface and the rear surface of the main flight in an arbitrary section between the metering zone A plasticizing apparatus, comprising: a screw provided with a ventilation portion including a notch provided in a width of only half of a main flight pitch interval only in a main flight in the vicinity of the front from a front portion of the main flight.
前記加熱筒へ供給する原料を制限制御する原料調節手段を備えたことを特徴とする請求項1に記載の可塑化装置。 2. The plasticizing apparatus according to claim 1 , further comprising a raw material adjusting means for restricting and controlling a raw material supplied to the heating cylinder. 請求項1または請求項2に記載の可塑化装置を用いた可塑化方法であって、
前記可塑化装置で設定可能な最大回転速度の50%以上の回転速度で前記スクリュを回転駆動するとともに、スクリュ背圧力を溶融材料の圧力において0〜5MPaの範囲で制御することを特徴とする可塑化方法。
A plasticizing method using the plasticizing apparatus according to claim 1 or 2 ,
The screw is driven to rotate at a rotational speed of 50% or more of the maximum rotational speed that can be set by the plasticizing apparatus, and the screw back pressure is controlled in the range of 0 to 5 MPa in the pressure of the molten material. Method.
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