JPS6265672A - Head apparatus of food-processing extruder - Google Patents

Head apparatus of food-processing extruder

Info

Publication number
JPS6265672A
JPS6265672A JP60207454A JP20745485A JPS6265672A JP S6265672 A JPS6265672 A JP S6265672A JP 60207454 A JP60207454 A JP 60207454A JP 20745485 A JP20745485 A JP 20745485A JP S6265672 A JPS6265672 A JP S6265672A
Authority
JP
Japan
Prior art keywords
outer circumferential
conical
die
flow path
cylinder
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.)
Pending
Application number
JP60207454A
Other languages
Japanese (ja)
Inventor
Katsumi Sugano
菅野 勝視
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.)
TECH RES ASSOC EXTRU COOK FOOD IND
Original Assignee
TECH RES ASSOC EXTRU COOK FOOD IND
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 TECH RES ASSOC EXTRU COOK FOOD IND filed Critical TECH RES ASSOC EXTRU COOK FOOD IND
Priority to JP60207454A priority Critical patent/JPS6265672A/en
Publication of JPS6265672A publication Critical patent/JPS6265672A/en
Pending legal-status Critical Current

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  • Formation And Processing Of Food Products (AREA)

Abstract

PURPOSE:To eliminate the troubles in the flow of molding material occuring at the conventional breaker plate such as nonuniform flow, stagnation, temperature unevenness, etc., by inserting a straightening mechanism having a particular structure between the die and the tip of a cylinder containing a screw. CONSTITUTION:A straightening mechanism 6 is inserted between the die 4 and the tip of a cylinder 2 containing a screw 3. The straightening mechanism is composed of the casing 20 and a core part 21 consisting of the front cone head 25 and the rear cone head 26 tapered at both ends and inserted into said casing 20. An annular channel group 32 consisting of a number of channels 34 arranged concentrically to the body part 24 is formed between the body part 24 and the casing 20 and between the front and rear cone heads 25, 26 of the core part 21. A back-tapered conical channel 33 is formed between the rear cone head 26 and the casing 20.

Description

【発明の詳細な説明】 (産業上の利用分野) 本発明は、主に食品加−「に使用される押出機のヘッド
装置に関する。
DETAILED DESCRIPTION OF THE INVENTION (Industrial Application Field) The present invention relates to an extruder head device mainly used for food processing.

(従来の技術) 例えば、ペットフート、飼料及びス→・・ツク食品等の
食品をす1率良く加圧する装置として、1本又は2本の
スクリュを包囲したシリンダの先端にダイ (又は類似
機構)を設けて構成されたl軸又は2軸の押出機がある
(Prior art) For example, a die (or similar mechanism) is installed at the tip of a cylinder surrounding one or two screws as a device for pressurizing foods such as pet food, feed, and food such as food. ) There are l-screw or twin-screw extruders configured with a

この押出機のヘッド装置はダイの他に整流構造体として
のブレーカプレートを設けて、シリンダから押動されて
くる材料を整流しながらダイから押出すように構成され
でいる。
The head device of this extruder is configured to include a breaker plate as a rectifying structure in addition to the die, so that the material pushed from the cylinder is extruded from the die while being rectified.

(発明が解決しようとする問題点) 前記従来のヘッド装置においては、ブレーカプレートの
略全面に材料流通孔が形成されており、繊維状の整流が
行なわれるが材*21の流動性が悪い場合には、ブレー
カプレートの一部、特に中央のみに流れが集中すること
があり、加工材ネlの流れの不均一、滞留、温度ムラ等
の問題が発生ずる。
(Problems to be Solved by the Invention) In the conventional head device described above, material flow holes are formed on almost the entire surface of the breaker plate, and fibrous rectification is performed, but when the fluidity of the material *21 is poor. In this case, the flow may concentrate only in a part of the breaker plate, especially in the center, causing problems such as uneven flow of the work material, stagnation, and temperature unevenness.

(問題点を解決するための手段) 本発明は、シリンダとダイとの間に配置される整流構造
体の内部に胴部とその前後の前後部円錐頭を有する中央
部を設け、この中央部の胴部と整流構造体の外周部との
間に環状群孔流路を、後部円錐頭と外周部との間に先細
り円錐流路を夫々形成し、材1’lを前部円錐Onで周
辺に均一分散して環状流にし、この環状流を一1多数本
に分化した後に再び環状流に戻すように構成することに
より、前記従来技術の問題点を解決できるようにしたも
のである。
(Means for Solving the Problems) The present invention provides a center portion having a body portion and front and rear conical heads on the front and rear sides of the body portion inside the rectifying structure disposed between the cylinder and the die. An annular group hole channel is formed between the body of the body and the outer periphery of the flow straightening structure, and a tapered conical channel is formed between the rear conical head and the outer periphery, and the material 1'l is connected to the front conical On. The problems of the prior art described above can be solved by uniformly dispersing the flow around the periphery to form an annular flow, dividing this annular flow into eleven or more, and then returning it to the annular flow.

即ち、本発明における問題解決手段の具体的構成の特徴
とするところは、スクリュ3を回転自在に包囲したシリ
ンダ2の先端とダイ4との間に整流構造体6を配置した
食品加工用押出機のへノド装置において、前記整流構造
体6はシリンダ2とダイ4との間に配置された外周部2
0と、この外周部20の内部に形成されていて前後に先
端先細り状の前部円錐頭25と後部円錐頭26とを形成
した中央部21とを有しており、前記中央部2Iの前後
部円錐頭25.26間の周部24と外周部20との間に
は胴部24と同心に多数の孔を環状に配列した環状群孔
流路32が形成され、前記後部円錐聞26と外周部20
との間には後方先細り状の円錐流路33が形成されてい
る点にある。
That is, the specific configuration of the problem-solving means of the present invention is characterized by an extruder for food processing in which a rectifying structure 6 is disposed between a die 4 and the tip of a cylinder 2 that rotatably surrounds a screw 3. In the Henoding device, the rectifying structure 6 has an outer peripheral portion 2 disposed between the cylinder 2 and the die 4.
0, and a central portion 21 formed inside this outer circumferential portion 20 and having a front conical head 25 and a rear conical head 26 with tapered tips in the front and rear, and the front and rear of the central portion 2I. An annular group hole channel 32 in which a large number of holes are arranged in an annular manner concentrically with the body part 24 is formed between the peripheral part 24 and the outer peripheral part 20 between the rear conical heads 25 and 26. Outer periphery 20
A conical flow path 33 tapering backward is formed between the two.

(作 用) スクリュ3によってシリンダ2から整流構造体6へ押出
された加工材料は、中央部21の前部円錐W425によ
って中央集中が阻止され、周辺へ略均−に分散されて環
状群孔流路32へ流れ込む。環状群孔流路32に流れ込
んだ材料は、番孔34に分離され、番孔34の流動抵抗
を受けて整流、配向作用を受ける。群化34を通過した
材料はあたかも環状に配列した繊維の状態になって円錐
流路33内に入り、この円錐流路33が先細りであるが
故に繊維状材料は環状が縮小するように合流し、増速し
ながら更に整流、配向作用を受けながらダイ4から出る
(Function) The processed material pushed out from the cylinder 2 to the rectifying structure 6 by the screw 3 is prevented from being concentrated in the center by the front cone W425 of the central part 21, and is almost uniformly dispersed to the periphery to form an annular group hole flow. Flows into road 32. The material that has flowed into the annular group hole channel 32 is separated into the holes 34, and is subjected to flow resistance of the holes 34 to be rectified and oriented. The material that has passed through the grouping 34 enters the conical flow path 33 as if it were fibers arranged in a ring shape, and since this cone flow path 33 is tapered, the fibrous materials merge so that the ring shape is reduced. , and exits from the die 4 while being further rectified and oriented while increasing its speed.

(実施例) 以下、本発明の実施例を図面に基いて説明する。(Example) Embodiments of the present invention will be described below with reference to the drawings.

第1.2図に示す第1実施例において、押出機1はボア
の内周壁が断面略8の字形のシリンダ2内に2本のスク
リュ3が回転自在に内蔵され、シリンダ2とダイ4との
間に、流路形成部材5及び整流構造体6が配置されてい
る。
In the first embodiment shown in FIG. 1.2, an extruder 1 has two screws 3 rotatably built into a cylinder 2 whose inner circumferential wall of the bore has an approximately figure-eight cross section. A flow path forming member 5 and a rectifying structure 6 are arranged between them.

8はシリンダ2の先端にボルト固定されたアダプタボデ
ィで、その内周側には流路形成部+A5 (ヘッドアダ
プタ)がスクリュ軸方向摺動自在に挿入され、そのフラ
ンジ部9に貫1ffiしたポル目0がアダプタボディ8
に螺合さねていζ、流路形成部材5の軸方向の位置を設
定している。
Reference numeral 8 denotes an adapter body bolted to the tip of the cylinder 2, into which a flow path forming part +A5 (head adapter) is inserted so as to be slidable in the axial direction of the screw. Eye 0 is adapter body 8
The axial position of the flow path forming member 5 is set by the screw thread ζ.

流路形成部材5内には2本のスクリュ3と同心の個別流
路12と、この各個別流路12のスクリュ側端部に形成
された円錐孔13と、両個別流路12の下流側に共通部
分としての溜り部14とが形成されている。
Inside the channel forming member 5, there are individual channels 12 concentric with the two screws 3, a conical hole 13 formed at the screw side end of each individual channel 12, and a conical hole 13 formed on the downstream side of both individual channels 12. A reservoir 14 is formed as a common part.

前記各円錐孔13はシリンダ2から突出しているスクリ
ュ3の円錐形先端3aと合致する形状であり、その上流
側の最大内i¥はスクリュ3を包囲するシリンダ2の孔
の内i¥と略一致していて、スクリュ3によって押出さ
れる材料が個別流路12へ円滑に流れ込むように形成さ
れている。この円錐孔13は円錐形先端3aと間隙15
を介し゛C対向しており、この間隙15が円錐管状流路
を形成している。前記間隙15はポル目0による流路形
成部材5のスクリュ軸線方向の位置調整によって大小に
任意に調整することができ、これにより、シリンダ2内
での圧力、混練度の調整並びに先端3aと円錐孔13と
の間で行なわれる剪断力の調整が可能になる。
Each of the conical holes 13 has a shape that matches the conical tip 3a of the screw 3 protruding from the cylinder 2, and the maximum inner i on the upstream side is approximately equal to the inner i of the hole of the cylinder 2 surrounding the screw 3. They are formed in such a way that the material extruded by the screw 3 flows smoothly into the individual channels 12 . This conical hole 13 has a conical tip 3a and a gap 15.
The gap 15 forms a conical tubular flow path. The gap 15 can be arbitrarily adjusted in size by adjusting the position of the flow path forming member 5 in the screw axis direction using the hole 0, thereby adjusting the pressure in the cylinder 2, the degree of kneading, and the distance between the tip 3a and the conical tip. It becomes possible to adjust the shearing force between the holes 13 and the holes 13.

前記溜り部14は断面円形の空間であり、前記2本の個
別流路12間から下流側へ尖端状に突出した潅流防止突
起16を有しており、2つの円錐孔13で絞られて個別
流路12を1lllってきた材料が降圧しながら合流す
る。
The reservoir part 14 is a space with a circular cross section, and has a perfusion prevention protrusion 16 that protrudes from between the two individual flow paths 12 in a tip shape toward the downstream side, and is narrowed by the two conical holes 13 so that the individual flow paths 12 are The materials that have come down the flow path 12 join together while decreasing the pressure.

流路形成部材5の下流側の整流構造体6は、外周部20
とその内部に一体成形された中央部21とを有する。外
周部20はストレート円筒状の第1ブロツク22と後方
(下流側)先細り円錐孔23aを有する第2ブロツク2
3とから成り、第1、第2ブロック22.23は流路形
成部材5に固定され、第2ブロツク23にはダイ4が固
定されている。
The flow regulating structure 6 on the downstream side of the flow path forming member 5 has an outer peripheral portion 20
and a central portion 21 integrally molded therein. The outer peripheral portion 20 includes a straight cylindrical first block 22 and a second block 2 having a rear (downstream side) tapered conical hole 23a.
The first and second blocks 22 and 23 are fixed to the channel forming member 5, and the die 4 is fixed to the second block 23.

前記中央部21はストレート筒状の胴部24の前後部に
先端先細り状の前部円錐tliJI25と後部円錐頭2
6とが一体形成されている。
The central portion 21 has a straight cylindrical body portion 24 with a front cone tliJI 25 having a tapered tip and a rear conical head 2 at the front and rear portions thereof.
6 are integrally formed.

前記外周部20及び中央部21の各内部は空洞になって
いて通路29a、29hを介して外部と連通しており、
熱媒体(加熱、冷却可能な媒体)が循環供給可能な温度
調節部28を形成しており、材料の温度調整を任意に且
つ内部まで均一に行うことができる。この温度調節部2
8は電気加熱手段(又はそれと熱媒体とを併用した加熱
手段)で構成しても良く、また、外周部20と中央部2
1の少なくとも一方にあれば良い。しかし、実施例の如
く、両部20゜21に加熱手段を設ければ、材料の内外
から同時に温度調整ができ、材11温度を均一りつ速や
かに、また微細に調整することができ、より高品質な製
品を得ることが可能になる。
The insides of the outer peripheral part 20 and the central part 21 are hollow and communicate with the outside through passages 29a and 29h,
A temperature adjustment section 28 is formed in which a heat medium (a medium that can be heated and cooled) can be circulated and supplied, and the temperature of the material can be adjusted arbitrarily and uniformly throughout the inside. This temperature adjustment section 2
8 may be constituted by an electric heating means (or a heating means using a heating medium in combination with the electric heating means), and the outer peripheral part 20 and the central part 2
It is sufficient if at least one of 1. However, if heating means are provided at both parts 20 and 21 as in the embodiment, the temperature can be adjusted from the inside and outside of the material at the same time, and the temperature of the material 11 can be uniformly, quickly, and finely adjusted, making it possible to achieve even higher temperatures. It becomes possible to obtain quality products.

中央部21の前部円8HJI25は、第1ブロツク22
よりも前方に突出していて流路形成部材5内に位置し、
流路形成部材5との間に断面積が漸次縮小する分散流路
31を形成している。中央部21の胴部24と第1ブロ
ツク22の外周部20との間には環状群孔流路32を形
成している。この環状群孔流路32は胴部24の軸線と
平行な孔34を環状に1つ周方向略等間隔に多数配列し
たものであり、環状の分散流路31から流動してきた材
yI−1は、缶化34に略均等に流れ込む。
The front circle 8HJI25 of the central part 21 is the first block 22.
protrudes further forward and is located within the flow path forming member 5,
A dispersion flow path 31 whose cross-sectional area gradually decreases is formed between the flow path forming member 5 and the flow path forming member 5 . An annular group hole channel 32 is formed between the body portion 24 of the central portion 21 and the outer peripheral portion 20 of the first block 22. This annular group hole flow path 32 has a large number of holes 34 parallel to the axis of the body 24 arranged in an annular manner at substantially equal intervals in the circumferential direction, and the material yI-1 flowing from the annular dispersion flow path 31 flows into the canning 34 almost evenly.

前記縦孔34は第2図に示すような1列に限らず、第3
図に示すように2列又はそれ以上の多列に形成しても良
く、その孔径及び数は種々選択することができる。また
、縦孔34間の肉はスパイダ部35となって外周部20
と中央部21を繋げて両者を一体成形可能にしているが
、外周部20と中央部21とを別個に形成し、その間に
縦孔34を形成したリング部材を嵌合して構成すること
もできる。
The vertical holes 34 are not limited to one row as shown in FIG.
As shown in the figure, the holes may be formed in two or more rows, and the diameter and number of holes can be variously selected. Further, the flesh between the vertical holes 34 becomes a spider part 35 and the outer peripheral part 20
Although the outer peripheral part 20 and the central part 21 can be integrally molded by connecting them, it is also possible to form the outer peripheral part 20 and the central part 21 separately and fit a ring member with a vertical hole 34 between them. can.

後部円錐頭26と外周部20の第2ブロツク23の円錐
孔23aとは対面していて先細り円錐流路33を形成し
ており、前記流路3]、 32.33は連通しており、
円錐流路33の後端はl孔に集束されてダイ4に連通し
ている。前記円錐流路33の間隙36は全長間−又は下
流側へ漸次狭くなるように形成されている。
The rear conical head 26 and the conical hole 23a of the second block 23 of the outer peripheral part 20 face each other to form a tapered conical channel 33, and the channels 3], 32, and 33 communicate with each other.
The rear end of the conical flow path 33 is converged into an l hole and communicates with the die 4. The gap 36 of the conical flow path 33 is formed so as to become gradually narrower along the entire length or toward the downstream side.

前記シリンダ2から押出された材料は、流路形成部材5
で圧縮・剪断が加えられた後に整流構造体6内に供給さ
れる。この整流構造体6に入る材料は前部円錐0n25
によって流れの中央築中が阻ILされ、周辺に分散され
て均一化し、環状縦孔流路32の孔34に流れ込む。こ
の環状群孔流路32はそのl−流に比べて狭い環状オリ
フィスとなっており、材11は多数本の繊維(丸棒)状
となって流動し、番孔34の壁面からI11別に流動抵
抗を受け、粘性流状の流速分布をして剪断力及び圧力を
発律し、流動方向に沿った配向、繊維化(配向が固定し
た状態)による組織化、性状改良が行なわれる。
The material extruded from the cylinder 2 is transferred to the flow path forming member 5
After being compressed and sheared at , it is supplied into the rectifying structure 6 . The material entering this rectifying structure 6 is the front cone 0n25
The central flow of the flow is blocked by this, the flow is dispersed to the periphery, becomes uniform, and flows into the hole 34 of the annular vertical channel 32. This annular group hole flow path 32 is a narrow annular orifice compared to the l-flow, and the material 11 flows in the form of many fibers (round rods), and flows from the wall surface of the hole 34 separately to I11. In response to resistance, a viscous fluid-like flow velocity distribution is generated to generate shearing force and pressure, and orientation along the flow direction, organization through fiberization (a state in which the orientation is fixed), and property improvement are performed.

環状群孔流路32を通過した材料は、拡大流路に、Lる
乱れや滞流が生しることなく円錐流路33に入り、環状
配列の流線が求心状に集合する縮流となる。
The material that has passed through the annular group hole flow path 32 enters the conical flow path 33 without any turbulence or stagnation in the expanded flow path, resulting in a contracted flow in which streamlines in an annular arrangement converge centripetally. Become.

この円&fll&路33でも組織化、+21状改良等の
整流作用は続けられ、材料は細流となるため流速増加及
び圧力増加を生じつつ、配向が更に強力に押し進められ
る。
In this circle & full & path 33, the rectifying action such as organization and +21 shape improvement continues, and since the material becomes a trickle, the flow velocity and pressure increase, and the orientation is further pushed forward.

そして円錐流路33iffi通後の材ネlは東京された
1本の繊維束状となってしかも略完全な整流状態でダイ
4に入り、配向組織が固定化されF]つ所望の賦形を受
けて押出される。
After passing through the conical flow path 33iffi, the material becomes a single fiber bundle and enters the die 4 in an almost completely rectified state, where the oriented structure is fixed and the desired shape is formed. It is received and pushed out.

このようにして加工された製品は、全断面均で且つ繊維
状の組織体となっており、食感が向1−する。
The product processed in this manner has a fibrous structure with a uniform cross section, and has a good texture.

第1図において、46.47はハンl′ヒータ、48は
材料温度耐を夫々示している。
In FIG. 1, 46 and 47 indicate the heater l' heater, and 48 indicates the material temperature resistance, respectively.

尚、前記第1実施例において、整流構造体6は整流形成
部材5を介在させずに、シリンダ2に泊接又はアダプタ
ボディ8を介して接続しても良く、また、外周部20を
Mit部円錐頭25の外方まで突出して分散流路31を
形成したり、第2ブロツク23内にIIM調用外用熱媒
体通路成して温度調節部を形成したりすることも可能で
ある。更に、流路形成部材5を設けない場合は、整流構
造体6はl軸押出機に適用することができる。
In the first embodiment, the rectifying structure 6 may be connected to the cylinder 2 through a vertical connection or an adapter body 8 without intervening the rectifying member 5, and the outer circumferential portion 20 may be connected to the mit portion. It is also possible to form a dispersion flow path 31 by protruding to the outside of the conical head 25, or to form an external heating medium path for IIM adjustment within the second block 23 to form a temperature control section. Furthermore, when the channel forming member 5 is not provided, the rectifying structure 6 can be applied to an l-axis extruder.

第4図は本発明の第2実施例を示しており、後部円錐頭
26の後端は尖端状でなく円柱状に形成され、筒状ダイ
4′内にはスパイダ38を介してマンドレル37が配置
され、このマンドレル37の前端は後部円錐凹26と固
定又は一体成形されている。
FIG. 4 shows a second embodiment of the present invention, in which the rear end of the rear conical head 26 is formed not in a pointed shape but in a cylindrical shape, and a mandrel 37 is inserted into the cylindrical die 4' via a spider 38. The front end of this mandrel 37 is fixed or integrally formed with the rear conical recess 26.

このヘッド装置は管状ダイ4′からパイプ状製品を押出
すものであり、パイプ状製品は1箇所以−Lに切り目を
入れることによりシート状にすることができる。尚、ダ
イ内部で材1’lをシート状に流動させ、シート状製品
を押出すようにすることも可能である。
This head device extrudes a pipe-shaped product from a tubular die 4', and the pipe-shaped product can be made into a sheet by making a cut at one point or more. It is also possible to flow the material 1'l into a sheet inside the die and extrude a sheet-like product.

第5.6図は本発明の第3実施例を示しており、外周部
20の第1ブロツク22、中央部21及び環状縦孔流路
32は前1&2分割されており、従って、温度関節部2
8を前1&2段に形成されており、独立調節可能になっ
ている。
FIG. 5.6 shows a third embodiment of the present invention, in which the first block 22 of the outer peripheral part 20, the central part 21 and the annular vertical hole channel 32 are divided into front 1 & 2 parts, so that the temperature joint part 2
8 is formed on the front 1st and 2nd stage, and can be adjusted independently.

前側の環状縦孔流路32Aは前記第1実施例と同様に孔
34が1列に形成されているが、後側の環状縦孔流路3
2t1は番孔34に対応して複数(例えば4つ)の小孔
34′が形成されており、孔34を通ってきた材料を更
に細分割して、より強力な整流、配量作用を行ない得る
ように構成している。
The annular vertical hole flow path 32A on the front side has holes 34 formed in one row as in the first embodiment, but the annular vertical hole flow path 32A on the rear side has holes 34 formed in one row.
In 2t1, a plurality of (for example, four) small holes 34' are formed corresponding to the number holes 34, and the material passing through the holes 34 is further divided into smaller parts to perform stronger rectification and metering action. It is configured to obtain.

尚、第1ブロツク22及び中央部21の各空洞に1枚以
上の中間壁を設けて温度調節部28のみを前後複数段に
分割することも可能である。
It is also possible to provide one or more intermediate walls in each cavity of the first block 22 and the central part 21 to divide only the temperature adjusting part 28 into a plurality of front and rear stages.

前記温度調節部28を材料流動方向に多段にすることに
より、環状縦孔流路32内を流れる材料の配向性、製品
性状を更に広範囲に調整でき、また、細分割縦孔流路3
2Bを形成することにより、材料をより細い繊維状に形
成でき、整流、配量作用を増強できる。
By configuring the temperature adjustment section 28 in multiple stages in the material flow direction, the orientation and product properties of the material flowing inside the annular vertical hole flow path 32 can be adjusted over a wider range, and the finely divided vertical hole flow path 3
By forming 2B, the material can be formed into thinner fibers, and the rectification and metering effects can be enhanced.

第7図は本発明の第4実施例を示しており、整流構造体
6はシリンダ2の先端に固定のアダプタボディ8に取付
けられており、このアダプタボディ8には流量調整機構
41が設けられている。
FIG. 7 shows a fourth embodiment of the present invention, in which the rectifying structure 6 is attached to an adapter body 8 fixed to the tip of the cylinder 2, and the adapter body 8 is provided with a flow rate adjustment mechanism 41. ing.

流量調整機構41はアダプタボディ8内に形成した環状
溝42に調整リング43を嵌入し、この調整リング43
の中心を3本以上のボルト44で中央部21の中心に対
して偏心調整可能にしている。
The flow rate adjustment mechanism 41 has an adjustment ring 43 fitted into an annular groove 42 formed in the adapter body 8.
The center of the center part 21 can be eccentrically adjusted with respect to the center of the central part 21 using three or more bolts 44.

前記調整リング43の内周面43aは胴部24の外周面
24aと間隙δを介して平行に対面しており、環状縦孔
流路32の直前に環状流路45を形成し、整流構造体6
の一部を構成している。調整リング43を押動して偏心
調整することにより、田部外周面24aとの周jノー 
1iil各I+7置ごの間隙δ、、δ2が変化し、その
間隙δを狭<′4゛ると流動抵抗は大きくなり材料流動
量が減少]る。
The inner circumferential surface 43a of the adjustment ring 43 faces the outer circumferential surface 24a of the body 24 in parallel with a gap δ therebetween, and forms an annular flow path 45 immediately before the annular vertical hole flow path 32, thereby forming a flow rectifying structure. 6
constitutes part of. By pushing the adjusting ring 43 and adjusting the eccentricity, the circumferential no.
The gaps δ, δ2 at each I+7 position change, and if the gaps δ are narrowed <'4, the flow resistance increases and the material flow rate decreases.

一般に、整流構造体6の各部に製1)誤差又は組合−誤
差等があるため、環状の流路3+、 32.33の周方
自省位置で流速を完全に均一にするごとは141罷であ
り、ダイ4から製品がlへ曲しながら押出されてくるの
で、調整リング43の位置調整で材*lの流(」に抵抗
を5えてII′1線状の製品が1甲山されるように修正
′4°る。
Generally, each part of the rectifying structure 6 has manufacturing errors or assembly errors, so it takes 141 strokes to make the flow velocity completely uniform at the circumferential self-reflection position of the annular flow path 3+, 32.33. , the product is extruded from the die 4 while bending in the direction l, so by adjusting the position of the adjustment ring 43, the resistance to the flow of material Correction '4°.

(発明のり」果) にλ1詳述した本発明によれば、整l々構造体6はシリ
ンダ2とダイ4との間に配置された外周部20と、この
外周部20の内部に形成さネ1でいて前後に先端先細り
状の前部円錐0125と後部円錐頭26とを形成した中
央部21とを自しており、前記中央部21の前後部内錐
卯25.26間の胴部24と外周部20との間には胴部
24と同心に多数の孔を環状に配列した環状群孔流路3
2が形成さね、前記後部円誰聞26と外周部20との間
には後ろ先細り状の円錐流路33がくる材¥−1を前部
用5M1iJ125によ−9て中央築中を阻+Lして周
辺に均一分散することができ、そして、その均一分散状
態で環状群孔流路32に流れ込むため、材料を細分化し
ながら均−nつ効果的な整流、配向作用を行なうことが
できる。また、材11が環状群孔流路32から先細り円
錐流路33へ流れると縮流となり、整流、配向作用を持
続又は増大することができる。従って、材ネlに流れの
不均一、滞留、温度ムラ等の問題を住しることなく、良
好1つ効果的な整流作用を加えることができ、高度に組
織化、性状改良された高品質の繊維状製品を製造するこ
とが可能になる。
(Results of the Invention) According to the present invention described in detail in λ1, the orderly structure 6 includes an outer circumferential portion 20 disposed between the cylinder 2 and the die 4, and a structure formed inside the outer circumferential portion 20. It has a central part 21 having a tapered front cone 0125 and a rear conical head 26 in the front and rear, and a body part 24 between the front and rear internal conical cones 25 and 26 of the central part 21. An annular group hole channel 3 in which a large number of holes are arranged in an annular manner concentrically with the body part 24 is provided between the outer peripheral part 20 and the body part 24.
2 is formed, and between the rear circular groove 26 and the outer peripheral part 20, a material ¥-1 with a rear tapered conical passage 33 is used with 5M1iJ125 for the front part to prevent the central construction. +L can be uniformly dispersed in the surrounding area, and since the uniformly dispersed state flows into the annular group hole channel 32, effective rectification and orientation can be performed while dividing the material into small pieces. . Further, when the material 11 flows from the annular group hole flow path 32 to the tapered conical flow path 33, the flow becomes contracted, and the flow rectification and orientation effects can be maintained or increased. Therefore, it is possible to add a good and effective rectification effect to the material without causing problems such as uneven flow, stagnation, and temperature unevenness, and it is highly structured and has a high quality with improved properties. It becomes possible to manufacture fibrous products of

また、外周部20及び中央部21の少なくとも一方に複
数段の温度調節部28A、28Bを形成することにより
、配向性、製品性状を更に広範囲に調整でき、更に、流
量調整機構41を設けるごとにより、より直線的な押出
製品を(することができる。
Furthermore, by forming multiple stages of temperature adjustment sections 28A and 28B in at least one of the outer circumferential section 20 and the central section 21, the orientation and product properties can be adjusted over a wider range. , a more linear extruded product (can be).

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

第1.2図は本発明の第1実施例を示しており、第1図
は縦断面図、第2191は第1図のn−n線断面図、第
3図は環状群化?Ai路の変形例を示す断面図、第4図
は第2実施例の要部を示す縦断面図、第5.6図は第3
実施例を示しており、第5図は要部の縦断面図、第6図
は第5図の■矢視図、第7図は第4実施例の要部を示す
縦断面図である。 1・・・押出機、2・・・シリンダ、3・・・スクリュ
、4・・・ダイ、6・・・整流構造体、20・・・外周
部、21・・・中央部、24・・・胴部、25・・・前
部円錐頭、26・・・後部円錐頭、28・・・温度調節
部、31・・・分散流路、32・・・環状群孔流路、3
3・・・円錐流路、41・・・流量調整機構。 特 許 出 願人 食品産業エクストルージョンクツキ
ング技術研究組合
Fig. 1.2 shows the first embodiment of the present invention, Fig. 1 is a longitudinal sectional view, Fig. 2191 is a sectional view taken along the line nn of Fig. 1, and Fig. 3 is annular grouping? A sectional view showing a modified example of the Ai path, FIG. 4 is a vertical sectional view showing the main part of the second embodiment, and FIG.
FIG. 5 is a longitudinal cross-sectional view of a main part, FIG. 6 is a view taken in the direction of the ■ arrow in FIG. 5, and FIG. 7 is a longitudinal cross-sectional view of a main part of a fourth embodiment. DESCRIPTION OF SYMBOLS 1... Extruder, 2... Cylinder, 3... Screw, 4... Die, 6... Rectifying structure, 20... Outer peripheral part, 21... Center part, 24...・Body part, 25... Front conical head, 26... Rear conical head, 28... Temperature adjustment section, 31... Dispersion channel, 32... Annular group hole channel, 3
3... Conical flow path, 41... Flow rate adjustment mechanism. Patent applicant: Food Industry Extrusion Shoes Technology Research Association

Claims (1)

【特許請求の範囲】 1、スクリュ3を回転自在に包囲したシリンダ2の先端
とダイ4との間に整流構造体6を配置した食品加工用押
出機のヘッド装置において、前記整流構造体6はシリン
ダ2とダイ4との間に配置された外周部20と、この外
周部20の内部に形成されていて前後に先端先細り状の
前部円錐頭25と後部円錐頭26とを形成した中央部2
1とを有しており、前記中央部21の前後部円錐頭25
、26間の胴部24と外周部20との間には胴部24と
同心に多数の孔を環状に配列した環状群孔流路32が形
成され、前記後部円錐頭26と外周部20との間には後
方先細り状の円錐流路33が形成されていることを特徴
とする食品加工用押出機のヘッド装置。 2、前記環状群孔流路32は材料流動方向に複数段に区
分されており、下流側環状群孔流路32Bは上流側環状
群孔流路32Aの各孔34に対応する複数の孔34′が
形成されていることを特徴とする特許請求の範囲第1項
に記載の食品加工用押出機のヘッド装置。 3、スクリュ3を回転自在に包囲したシリンダ2の先端
とダイ4との間に整流構造体6を配置した食品加工用押
出機のヘッド装置において、前記整流構造体6はシリン
ダ2とダイ4との間に配置された外周部20と、この外
周部20の内部に形成されていて前後に先端先細り状の
前部円錐頭25と後部円錐頭26とを形成した中央部2
1とを有しており、前記中央部21の前後部円錐頭25
、26間の胴部24と外周部20との間には胴部24と
同心に多数の孔を環状に配列した環状群孔流路32が形
成され、前記後部円錐頭26と外周部20との間には後
方先細り状の円錐流路33が形成されており、前記外周
部20及び中央部21の少なくとも一方には材料流動方
向に複数段の温度調節部28が形成されていることを特
徴とする食品加工用押出機のヘッド装置。 4、スクリュ3を回転自在に包囲したシリンダ2の先端
とダイ4との間に整流構造体6を配置した食品加工用押
出機のヘッド装置において、前記整流構造体6はシリン
ダ2とダイ4との間に配置された外周部20と、この外
周部20の内部に形成されていて前後に先端先細り状の
前部円錐頭25と後部円錐頭26とを形成した中央部2
1とを有しており、前記中央部21の前後部円錐頭25
、26間の胴部24と外周部20との間には胴部24と
同心に多数の孔を環状に配列した環状群孔流路32が形
成され、前記後部円錐頭26と外周部20との間には後
方先細り状の円錐流路33が形成されており、前記整流
構造体6の環状群孔流路32の前方には、環状群孔流路
32に入る材料の周方向各位置での流動抵抗を調整する
流量調整機構41が設けられていることを特徴とする食
品加工用押出機のヘッド装置。
[Claims] 1. In a head device for a food processing extruder in which a rectifying structure 6 is disposed between a die 4 and the tip of a cylinder 2 that rotatably surrounds a screw 3, the rectifying structure 6 is An outer circumferential portion 20 disposed between the cylinder 2 and the die 4, and a central portion formed inside the outer circumferential portion 20 and having a front conical head 25 and a rear conical head 26 with tapered ends in the front and rear. 2
1, and a front and rear conical head 25 of the central portion 21.
, 26 is formed between the body part 24 and the outer circumferential part 20, there is formed an annular group hole channel 32 in which a large number of holes are arranged in an annular manner concentrically with the body part 24. A head device for an extruder for food processing, characterized in that a conical channel 33 tapering backward is formed therebetween. 2. The annular group hole channel 32 is divided into multiple stages in the material flow direction, and the downstream annular group hole channel 32B has a plurality of holes 34 corresponding to each hole 34 of the upstream annular group hole channel 32A. 2. The head device of an extruder for food processing according to claim 1, wherein the head device is formed with: . 3. In a head device for a food processing extruder in which a rectifying structure 6 is disposed between the tip of a cylinder 2 that rotatably surrounds a screw 3 and a die 4, the rectifying structure 6 is arranged between the cylinder 2 and the die 4. an outer circumferential portion 20 disposed between the outer circumferential portion 20 and a central portion 2 having a front conical head 25 and a rear conical head 26 formed inside the outer circumferential portion 20 and having tapered ends in the front and rear directions;
1, and a front and rear conical head 25 of the central portion 21.
, 26 is formed between the body part 24 and the outer circumferential part 20, there is formed an annular group hole channel 32 in which a large number of holes are arranged in an annular manner concentrically with the body part 24. A conical flow path 33 tapering backward is formed between the two, and a plurality of temperature adjustment sections 28 are formed in at least one of the outer peripheral part 20 and the central part 21 in the material flow direction. Head device for extruder for food processing. 4. In a head device for a food processing extruder in which a rectifying structure 6 is disposed between the tip of a cylinder 2 that rotatably surrounds a screw 3 and a die 4, the rectifying structure 6 is arranged between the cylinder 2 and the die 4. an outer circumferential portion 20 disposed between the outer circumferential portion 20 and a central portion 2 having a front conical head 25 and a rear conical head 26 formed inside the outer circumferential portion 20 and having tapered ends in the front and rear directions;
1, and a front and rear conical head 25 of the central portion 21.
, 26 is formed between the body part 24 and the outer circumferential part 20, there is formed an annular group hole channel 32 in which a large number of holes are arranged in an annular manner concentrically with the body part 24. A conical flow path 33 tapering backward is formed between them, and in front of the annular group hole flow path 32 of the flow straightening structure 6, there is formed a conical flow path 33 at each position in the circumferential direction of the material entering the annular group hole flow path 32. 1. A head device for an extruder for food processing, characterized in that a flow rate adjustment mechanism 41 is provided to adjust the flow resistance of the food processing extruder.
JP60207454A 1985-09-18 1985-09-18 Head apparatus of food-processing extruder Pending JPS6265672A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP60207454A JPS6265672A (en) 1985-09-18 1985-09-18 Head apparatus of food-processing extruder

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP60207454A JPS6265672A (en) 1985-09-18 1985-09-18 Head apparatus of food-processing extruder

Publications (1)

Publication Number Publication Date
JPS6265672A true JPS6265672A (en) 1987-03-24

Family

ID=16540034

Family Applications (1)

Application Number Title Priority Date Filing Date
JP60207454A Pending JPS6265672A (en) 1985-09-18 1985-09-18 Head apparatus of food-processing extruder

Country Status (1)

Country Link
JP (1) JPS6265672A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2001000164A (en) * 1999-04-30 2001-01-09 Soc Prod Nestle Sa Extrusion die
US11756698B2 (en) 2007-11-15 2023-09-12 Nuscale Power, Llc Passive emergency feedwater system

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2001000164A (en) * 1999-04-30 2001-01-09 Soc Prod Nestle Sa Extrusion die
JP2010259441A (en) * 1999-04-30 2010-11-18 Soc Des Produits Nestle Sa Extrusion die
JP4616967B2 (en) * 1999-04-30 2011-01-19 ソシエテ・デ・プロデュイ・ネスレ・エス・アー Extrusion die
US11756698B2 (en) 2007-11-15 2023-09-12 Nuscale Power, Llc Passive emergency feedwater system

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