JPS5829644A - Air deflation pushing by twin-screw extruder - Google Patents
Air deflation pushing by twin-screw extruderInfo
- Publication number
- JPS5829644A JPS5829644A JP56127264A JP12726481A JPS5829644A JP S5829644 A JPS5829644 A JP S5829644A JP 56127264 A JP56127264 A JP 56127264A JP 12726481 A JP12726481 A JP 12726481A JP S5829644 A JPS5829644 A JP S5829644A
- Authority
- JP
- Japan
- Prior art keywords
- air
- opening
- screw
- supply port
- powder
- 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.)
- Granted
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
- B29C48/76—Venting, drying means; Degassing means
- B29C48/765—Venting, drying means; Degassing means in the extruder apparatus
- B29C48/766—Venting, drying means; Degassing means in the extruder apparatus in screw extruders
- B29C48/767—Venting, drying means; Degassing means in the extruder apparatus in screw extruders through a degassing opening of a barrel
-
- 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)
- Extrusion Moulding Of Plastics Or The Like (AREA)
Abstract
Description
【発明の詳細な説明】
不兄明O工1°At−へ合ノ聾四方間In1転押出4幾
に係り、同押出磯の原料供給口よりバ1/ル内・に1t
t給さねろ1)茂扮体原p’l i’r包含さハる空気
を1友く押出方法に関する。[Detailed Description of the Invention] Concerning the four-way In1 transfer extrusion of the Fuei Akira 1 degree At- to 4-way In 1 turn extrusion, 1 ton per barrel from the raw material supply port of the same extrusion
1) Relating to a method for extruding air containing air.
従来から見かけ比重が小さい微粉体樹脂もしくは同様の
無機微粉体を多量に含むプラスチック材料などを押出1
ist形するとき押出機供給部における原XSIθ)喰
い込み量が押出量を限定する場合が多い。Extrusion of plastic materials containing a large amount of fine powder resin or similar inorganic fine powder with a small apparent specific gravity has traditionally been carried out.
When ist-forming, the amount of feed into the original XSI θ) in the extruder supply section often limits the extrusion amount.
こ才1を解決する手段として例えば強制供給装置(コン
パクタ)を使用することは周知である。しかしコンパク
タを使用しても非常VC細かい粒子で1;−il、かけ
叱■1(≠しトさく流動化(bl旧dizing) L
易すい粉末ではその効果は完全で(工なく所′¥1θ)
押出量をf脣ることは!l!、I# L、 <限らねた
範囲の押出条件で運転するしか′f′、Cかった。It is well known to use, for example, a forced feeding device (compactor) as a means of solving this problem. However, even if a compactor is used, very fine particles of VC will be produced.
The effect is complete with easy-to-clean powders (without effort ¥1θ)
The amount of extrusion can be reduced by f! l! , I# L, <It was only possible to operate under a limited range of extrusion conditions.
こ0)よつTx i’;a粉体の’−It給部にお(す
る喰い込みを妨げている最大の要因は見かけ比J【が小
さい故I(微粉体が色量する多量の空気でありこσ)空
気を多量に含んだ材を1が押出4畿内で圧縮され空気を
分離し、その空気はホッパ側音、すなわち材料の移動方
間と逆に流ねその結果バレル内で微粉体が流動状j、I
ηと7:Cるためである。そのために材料θ)見かげ)
納優係叔が小さく Icり粉末のスクリュによる圧縮ブ
バおこりにくくなりその結果スクリュ本来の+72r
171輸送量は低下する。く)ちろんこθ〕場合にもバ
レルからθ> ;Jn熱によって材料は加熱さl欧化し
、スクリュによるワ1j断刀とあいまって圧縮浴融(1
伍?−r1°−る1こめ押出作用は失わね、/fいが、
押11)1悶木米の磯1重である材料を圧縮し主と(−
て機械的r「すfJ断発熱1(よりm酬さぜることより
イ()らハる111’ lI:t ニアiと(工(まる
か(で低い亜力しか距揮でλf(′い。The biggest factor preventing the powder from being bitten into the '-It feeding section is the small apparent ratio J σ) A material containing a large amount of air is extruded. It is compressed in the four ridges and the air is separated, and the air causes hopper side noise, that is, it flows in the opposite direction to the direction of movement of the material, resulting in fine powder in the barrel. Body is fluid j, I
This is because η and 7:C. Therefore, the material θ) appearance)
The compression ratio is smaller, and the compression caused by the screw of Ic powder is less likely to occur, resulting in the original +72r of the screw.
171 transportation volume will decrease. Even in the case of θ〕 from the barrel, the material is heated and melted by the heat, and combined with the cutting of the screw by the screw, the material is melted in the compression bath (1
Go? -r1°-r1 The extrusion effect is lost, /f, but
Press 11) Compress the material, which is one layer of 1-goku rice, and press (-
Mechanical r'sfJ intermittent heat generation 1 stomach.
本発明はかかる問題をifl’6決する方法で友、って
(衣粉体の包御する空気を押出促θ)供給口に哨流させ
ずこれらの包含空気を供給口の下流に設けた放11+口
より逃丁ことによって粉と空気の相対速度を滅失さぜ流
動化状態(Cさせずに押出てことによっで従来かl”)
’M1t、点とされていた前:i田111題を改善1
〜押出計の1曽大?果てことを目的とした新しい押11
4方法で゛ある。The present invention solves this problem by a method (for extruding the air contained in the coating powder θ), which eliminates the flow of trapped air to the supply port and provides a discharge outlet downstream of the supply port. 11+ The relative velocity of the powder and air is lost by releasing the powder from the opening, resulting in a fluidized state (conventional method by extruding without C)
'M1t, before it was considered as a point: Ida 111 problems improved 1
~One-largest extrusion meter? A new push 11 aimed at ending
There are 4 ways.
次に本発明による1′:Xが11例ケアJJ、 1図π
、1:り詣1明すると、1Qエニl1l111理出(幾
でバレル2内にスクリュ3が〃いに噛合、同方間回転し
ている。ll&工原」;・I供給口、5は、前記原料供
ホ110の下流に設はた空気抜き開1コ部である。6は
ベント孔である。前記スクリュ3には供給された原料を
浴解し、混練を行つ混練要素7が原511」供給口4と
空気抜き開1」部5の曲に設けである。11′5!扱う
材料は人別して下記の24申M:1’lが考えら、Jl
、
1)1散粉体4A’ 、1’)がプラスチック又Qまそ
の他θ)有機体の場合。Next, 1':X according to the present invention is 11 cases care JJ, 1 figure π
, 1: After visiting 1, 1 Q Enil 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 This is an air vent opening 1 located downstream of the raw material feeder 110. 6 is a vent hole.The screw 3 has a kneading element 7 for melting and kneading the supplied raw materials. The supply port 4 and the air vent opening 1" are provided in the section 5. 11'5! The materials to be handled are classified according to the person and the following 24 types M: 1'l are considered, Jl
, 1) When the powder 4A', 1') is plastic, Q or other θ) organic material.
2)政扮体相ボー1プバ無磯物で、プラスチック材料と
川に混練1−る場合。2) When the political body is mixed with plastic material and the water is mixed.
で゛ある。It is.
前者Z・ま倣扮体材料が未溶融状態θ)土又空気抜キ1
jibIrl ’ISに至るとある程度圧縮を受け、流
動化してい々〕I’′I1.扮体及び訓熱さねた空気&
′f、空気抜き開口部で急激に開放状態となるため、前
記空気抜き開口部I3より1吹き」二す易い。The former Z-Ma imitation body material is in an unmelted state θ) Tsuchimata air bleed 1
jibIrl 'When it reaches IS, it is compressed to some extent and becomes fluid]I''I1. The air of disguise and training heat &
'f, since the air vent opening is suddenly opened, it is easier to blow one blow from the air vent opening I3.
後者はプラスチック材料が未溶融で無機物と光分に混合
していない状帖(J)ま又空気吸き孔開口部に到達でろ
と未溶融プラスチック材料はIjn記開口開口部ントア
ップと同様σ)現象が起き、前記無機1散紛1本(工前
者と同様を前記開口部より吹き上ってし市つ。The latter is a phenomenon in which the plastic material is unmelted and not mixed with inorganic matter and light (J), and the unmolten plastic material reaches the air intake hole opening (σ), similar to the phenomenon described in Ijn. This caused the inorganic powder (similar to the former one) to blow up from the opening.
このよつに倣吻体ブバいず第1θ)場合であってイ)バ
レル内θ)プラスチック材料が未俗fA’l!状1.Q
:、θ)城で二′)t′気抜ぎ開口部を設けても空気θ
〕ツノ、を分ズ11シて+111出てることが出来ブ、
Cい。In this case, the proboscis body is the first θ) and the plastic material inside the barrel is vulgar fA'l! Condition 1. Q
:, θ) Even if a vent opening is provided in the castle, the air θ
] Tsuno, I was able to get +111 by getting 11 minutes,
C.
空気θ)みを分離し排出さ1上ろたソ)lcは、空気抜
き1iF40部にr+1達する前にプラスチックA’4
’ 、4’lヲ;e)7゜程V溶欣状弗とさぜ71′【
げ)1.はlr「〕ない。そこで前辺3(71よりに1
;攻紛[本/J)フ“ラスチック+gtlθ)1易合(
工1:タ勿体を溶融させイ)だぬり)混練′乃素7が涼
1に11it: +Tl’i’7 n4よりを気膜き;
フ;打]部5の間で心積と1「ろ。また做粉体が、IJ
?、炎1第18≧1.0)場合(・ま、プラスチックA
A伺ヲ箔帽(fると共(C′+7!η成倣粉体とある稈
汲混ぜ合わぜるためθ)前記混沖要素7/バ同様に11
1〔不′1供給「14ど空気1友きIJ110部50間
に必゛玖と/[ろ。た■しここテ11r f)T、r
コトfjニスクリ、:1− :3 Vcfr’i ?A
’ltあるいは/47; A東のための要素7を便用す
るがプラスチックLIi・・1/Iζこθ〕要素7部分
でバレル2の断Tm内に完全6て光/AI −4−ろよ
つな区域ケ設けたり材f・1Vc7−1[、強いj口部
を75えろよつy、c−fi−圧波を設げA゛に#;i
A!Itあるいは混練を行うよつにしなくてはならない
。さもないと空気は[;旧]部に至らず原料・ば給口に
逆流してしまう。The air θ) was separated and discharged, and the plastic A'4
' , 4'lwo; e) 7° V fusion shape 弗 and saze 71' [
Ge)1. is lr "]. Therefore, the front side 3 (1 by 71)
; Conflict [Book/J) Plastic + gtlθ) 1 easy combination (
Process 1: Melt the tamutai a) Danuri) Knead 'nomoto 7 to cool 1 11it: +Tl'i'7 From n4, make a film;
Between part 5 and part 5, the powder is IJ.
? , Flame 1 No. 18 ≧ 1.0) (・Ma, Plastic A
A: Foil cap (with f (C' + 7! η to mix the imitation powder with a certain culm, θ)) Mixed offshore element 7/Ba same as 11
1 [Un'1 supply "14 air 1 friend IJ110 part 50 must have /[ro. takashi kokote 11r f) T, r
Koto fj niskuri, :1- :3 Vcfr'i? A
'lt or /47; Use element 7 for A east, but plastic LIi... 1/I Provide a connecting area and create a strong j mouth part 75, c-fi-pressure wave on A゛#;i
A! It must be possible to carry out kneading or kneading. Otherwise, the air will not reach the [;old] section and will flow back into the raw material/gas supply port.
本発明[おいて圧縮部とは大質的・にスクリュ内シバ祠
事゛]1(より完全に発温(−ている部分を指し、スク
リュ3 VcよるfE縮はl【<ても例えば加熱により
部分的に材料が膨張してスクリュ3θ)溝を密に発温1
−だ場合に、そQ〕ような部分を圧縮部と見倣丁もので
ふる。In the present invention, the compressed part refers to the part where the screw is heated to a large extent. As a result, the material partially expands, causing the screw 3θ) groove to become densely heated1.
- If so, shake such a part with a compression part and a copy knife.
従ってバレル2内に材料が完全に発温てることなく前記
空気抜き開口部5から」二流に向ってガスは流ね、るよ
つに構成されている。このようなことを有効に行うため
のスクリュ形状については掘該業者にとって周知のこと
である。同方向lOJ転噛合形X・Ill+押出機では
一般にスクリュ溝深さには第2図て不丁ように全長にわ
たってほぼ一定であり、スクリュ形態にからくる圧縮I
11.第1図の矢線3aおよび7で示てよつにピッチP
の変化により行わfする。この」:うなものの※重送能
力についてQ工、例えは文献An Analysis
of the Coveying Character
is−tics of Twin−8crew Co−
Rotating Extruders、の第14図に
記載さJlている。Lつ(1て、スクリュ構内の桐材の
充ldル1率εに比例i−で輸送J、′IQ1111大
I−1同11テ1fでスクリュのネ/し角φとしてco
sφニ11″、例才ろ、ここでスクリュ中において1i
il記開口部5と供給1]・1との間で実′t1的it
こガス流が封止されイ、)ことのないよう・′Lfろた
めには、開口1・91(5と供給「1)1間の任意の位
i[tにおいて前述した光d、i、i率εプノi1以下
になろよう7xφ或い(工ビソチをiJ’A 41<
−r )1ばJ二い。さらに溝深りか変る場合も同様に
して求y)た輸送)け(でついてtr#4率さく1であ
るようKてハはよい。Therefore, the material in the barrel 2 is not completely heated, and the gas flows from the air vent opening 5 toward the second stream. The screw shape for effectively accomplishing this is well known to excavators. In the same direction lOJ rotary intermeshing type
11. Pitch P as shown by arrows 3a and 7 in FIG.
This is done by changing f. ``This'': Regarding the multi-feeding ability of Umono, Q Engineering, for example, refer to the literature An Analysis.
of the CoveyingCharacter
is-tics of Twin-8crew Co-
Rotating Extruders, shown in FIG. 14. L (1, transport J in proportion to the filling rate ε of paulownia wood in the screw premises, 'IQ1111 large I-1 same 11te 1f, co as the angle φ of the screw
sφ Ni 11'', as usual, here in the screw 1i
Between the opening 5 and the supply 1].
In order to prevent this gas flow from being sealed, the above-mentioned light d, i, Let's make the i rate ε Puno i1 or less 7xφ
-r) 1 ba J 2 ii. Furthermore, even if the groove depth changes, it is possible to calculate the transport value in the same manner so that the tr#4 ratio is 1.
ち
な饗前記文献の1商道量は溶削(体についてのもので訊
ろが、固体すこついても充A:’a率r((“ついて(
1同)’、:Q hc4又扱つことができる。Incidentally, the amount of 1 trade in the above literature is melting (I asked about the body, but even if there is some solid material, it is full A:'a rate r(("Tsuki(
1)', :Q hc4 can also be handled.
上記の説明において江意丁べきことシエ、−1投にプラ
スチック9工押出磯に供、爾さ」1押出(穴内で第1図
において原料供給口4→スクリユ3 a−)混7速要素
7の+11Mに仇′r1シてい<11異(ヤで゛、バレ
ル2か「)の1′J日熱あるいはスクリュ3からのり1
j 11ノ’T力にJ′、ろ14t]祭発熱′f、cど
により幅度が上昇しその結果多孔1ト1の粉体や、内部
の気孔内rこ水分その1mガスを含んでい石粉粒体1c
どでは、嵩比重が増大するために、容漬輸送計が大きく
なって同一スクリュ寸法では充満率εミ1となり閉塞状
態になることもあり得る。In the above explanation, it should be noted that the plastic 9 extrusion is carried out in 1 throw, and 1 extrusion (in the hole in Figure 1, raw material supply port 4 → Screw 3 a-) mixed 7-speed element 7 1'J solar heat or glue 1 from screw 3 if +11M of +11M <11 difference (Y, barrel 2 or ")"
j 11'T force J', filtration 14t] The width increases due to heat generation'f, c, etc., and as a result, the pores contain powder of 1 to 1, moisture in the internal pores, and 1 m of gas. Stone powder granule 1c
In other cases, since the bulk specific gravity increases, the container transport meter becomes larger, and with the same screw size, the filling rate becomes εmi1, which may lead to a blocked state.
このよつな状態においても空気抜き開口部5と供給口4
間の閉塞を生じさせないように、彩当てる部分をさく1
となるようスクリュの荷深さh、ピッチPを選択をでる
ことは、当該業者には容易にできることである。また文
献プラスチックエージ77−2.870にある混線用同
方向lr!J転場軸転出軸押出機1■)の構造と%1徽
に記載されているように、スクリュピッチの異るスクリ
ュエレメントの組立Vこよる構造をもっている押出機で
は、実際に閉塞する部分のスクリュエレメントをよりピ
ッチの大きf、cものに交換することによっても達成で
きろ。Even in this condition, the air vent opening 5 and the supply port 4
Cut out the part to be painted so as not to cause any blockage between the parts 1
It is easy for the person concerned to select the loading depth h and pitch P of the screw so that . Also, the same direction lr for crosstalk in the document Plastic Age 77-2.870! As described in the structure of J-transforming shaft-transferring-shaft extruder 1) and %1, in an extruder with a structure in which screw elements are assembled with different screw pitches, the part that actually closes is This can also be achieved by replacing the screw elements with ones with larger pitches f and c.
何れ1″てしても二軸押出機vcおいては区間前記開口
g35と供給口4でグラスチック材料でガス流が封11
−さti、 ’r、cいよつなスクリュ形状の1人定或
いはそのよう′IIc運転条件を、本来押出機に安来さ
几る混線条件、その他の押出条件から著しく外寸1.る
ことなく選定−fろことば、困難な〈実施することがで
きろ、
縮開)を設けるかぐンかであり、仮に空気抜き開口部に
てベントと同等の減圧を打ったんrらは昇比域がないた
め原料供給口と〕1ト1じ畝粉体を吸込むことVcなり
〕Ifj ’+%のベントは小町a「である、本発明は
グラスチック材料の11■頚と、そハに1鋤したスクリ
ュを溝1#: l−たうえで、Jjζ切な位置に開口部
を設置途てることにょリバレル内の空気を自然に外へ排
出させろことが出来る。In the twin-screw extruder VC, the gas flow is sealed with a glass material at the opening g35 and the supply port 4 in the section 11.
-Sti,'r,cThe external dimensions are significantly smaller than the one-person setting of the small screw shape or such 'IIc operating conditions due to cross-circuit conditions and other extrusion conditions that are originally difficult for the extruder. In other words, it is difficult to set up a difficult (possible to implement, retraction), and if we were to reduce the pressure at the air vent opening to the same level as a vent, the ratio would rise. Since there is no raw material supply port and one to one ridge powder is sucked in Vc] Ifj' + % vent is Komachi a', the present invention is the 11 neck of the glass material, After inserting the plowed screw into the groove #1, you can set the opening at the correct position to allow the air inside the barrel to naturally drain out.
次に本発明に、J:ろ実施制令′下記に21< ’ij
。Next, in accordance with the present invention, J:RO Implementation Regulations' below 21<'ij
.
実施例1゜
押出機 : 東芝機械製 1櫨み金型同方向1ρII+
云二輔押出磯、形式TEM−刃 スク
リュ径53φ
ノ矢 料 : ポリマー十伸((浅1散扮(、+: <
Vl、かげ比(75!t%) (15,41,+1
1.)軍0.05 )
押出イ幾の供給口にポリマーと無慎威粉体を各(9)
々別々の定縫供給装置を期用して同時投下した。Example 1゜Extruder: Toshiba Machine Co., Ltd. 1 zigzag mold same direction 1ρII+
Yunjisuke extrusion, type TEM-blade screw diameter 53φ
Vl, shadow ratio (75!t%) (15, 41, +1
1. ) 0.05 ) Polymer and powder powder were simultaneously dropped into the supply port of the extruder (9) using separate fixed stitch feeding devices.
結 果 : (イノ 空気抜き開口部のない場合、最大
押出−酢90 Ky/丁■
(ロ)空気抜き開口部を設H゛た場合、最大押出量1.
75 K9/H
いずね、の場合もスクリュ回転数
60Or、p、m
実施1列2
押出機 : 東芝機械製 噛み合1w同方向回転二輛押
出磯、形式TEM−100ス
クリュ径94φ
原 旧 、 スチレン系2粉体十無吸敵粉体(50重I
;T係)(50重−1幅)
いすねも200メツシュ通過したも
のでプリブレンド品(児かげ比重
0.5)で816゜
結 果 : (イj 空気抜穴開口部無し 岐大押出1
汁30oK9/rx
(口j 空気抜き開口部有り 1瞳大Pf1出fii
750 IFQ /lI
スクリュ回転奴ば300 r、p、m
以上の結果か「)も明1もかγCJつに、1)茂粉体1
1;1ネ−1の押出性(工従来l云に比べ大Ill ’
/、C’I’i’i覇“九り171ね、約2倍の押出量
プJ昌ア、「)ねる。Results: (INO: Maximum extrusion amount when there is no air vent opening - Vinegar 90 Ky/T) (b) When an air vent opening is provided, the maximum extrusion amount is 1.
75 K9/H Izune, screw rotation speed 60 Or, p, m Execution 1 row 2 Extruder: Manufactured by Toshiba Machine, meshing 1w co-rotating two-car extrusion rock, type TEM-100 screw diameter 94φ original old, Styrene-based 2-powder 10% absorbent powder (50 weight
; T section) (50 weight - 1 width) Isune also passed 200 mesh, pre-blended product (child shadow specific gravity 0.5) 816° Result: (Ij No air vent opening Kidai extrusion 1
Juice 30oK9/rx (mouth j with air vent opening, 1 pupil size Pf1 output fii
750 IFQ /lI Screw rotation part 300 r, p, m Is it the result of the above?
1:1 extrudability (higher extrudability than conventional technology)
/, C'I'i'i Ha"9 171, about twice the extrusion amount, ").
また原泊トπ、[つて9まそJl、 1ソ、ヒの効果−
h<lυ1侍出来る。Also Haramari To π, [Tsute 9 Maso Jl, 1 So, Hi effect-
h<lυ1 Samurai can do it.
4(図■のt8iロ1i7j説明
;君1図(・工本発明の1実施例を示同−図、7身12
図(ニスフリユの説明図。4 (Explanation of Fig.
Diagram (Explanatory diagram of Nisfuryu.
2・・・バレル、3・・スクリュ、4 ・原71(i”
pq71m、5・・・空′λ抜キ開ロ部、
出IQn人 東芝俵械沫Jに六刊
(1])
ネ 1 jz
f’21,12... Barrel, 3... Screw, 4 ・Hara 71 (i"
pq71m, 5...Empty 'λ removal opening part, output IQn person Toshiba Tawara Machinery J 6th issue (1]) Ne 1 jz f'21,1
Claims (1)
1cc包含< 7)空・気を01出てるための開[]部
を111・’、I Iyp Jソ、に設け、前記材狽1
.111.袷口と開口部θ)曲に4」、1・1ケ溶if
1’(イ、1−<Q工l昆線させるためのC昆利乏゛〃
素を111u女るブバ、その曲にて材料がバレル内C・
ζ光Tj4 L 石(いよう、YLcL、前記材料中に
色量さJする空気を前記開口j%より抜くことを’t?
I散と1−ろに攻扮体材filの空気因キti11出
方l〕みdownstream 0) barrel π front r+r +g(・
1cc included < 7) Provide an opening [] part for air/air to come out at 111・', I Iyp J So, and
.. 111. The sleeve opening and the opening θ) 4", 1.1 pieces if
1' (I, 1-<C kunri deficiency゛〃 to make Q engineering kun line
In the song, the material is C・
ζ Light Tj4 L Stone (Iyo, YLcL, don't you want to extract air of color amount J from the material through the opening j%?
The air factor of the attack body material fil in I-san and 1-ro is the way it appears.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP56127264A JPS5829644A (en) | 1981-08-13 | 1981-08-13 | Air deflation pushing by twin-screw extruder |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP56127264A JPS5829644A (en) | 1981-08-13 | 1981-08-13 | Air deflation pushing by twin-screw extruder |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS5829644A true JPS5829644A (en) | 1983-02-21 |
JPH021650B2 JPH021650B2 (en) | 1990-01-12 |
Family
ID=14955721
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP56127264A Granted JPS5829644A (en) | 1981-08-13 | 1981-08-13 | Air deflation pushing by twin-screw extruder |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS5829644A (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2002086542A (en) * | 2000-09-13 | 2002-03-26 | Tokyo Printing Ink Mfg Co Ltd | Extrusion molding method by twin-screw extruder |
US10676603B2 (en) | 2015-07-16 | 2020-06-09 | The Japan Steel Works, Ltd. | Method for producing resin composition |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN104105580A (en) | 2012-02-07 | 2014-10-15 | 三菱丽阳株式会社 | Resin mixture fabrication method |
Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS512770A (en) * | 1974-06-28 | 1976-01-10 | Ikegai Iron Works Ltd | Tajikuoshidashikino sukuryuu |
JPS51138748A (en) * | 1975-05-28 | 1976-11-30 | Japan Steel Works Ltd | Device for mixing and melting plastic compound material |
JPS53129374A (en) * | 1977-04-18 | 1978-11-11 | Japan Steel Works Ltd:The | Double-shaft kneading and deairing extruder |
-
1981
- 1981-08-13 JP JP56127264A patent/JPS5829644A/en active Granted
Patent Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS512770A (en) * | 1974-06-28 | 1976-01-10 | Ikegai Iron Works Ltd | Tajikuoshidashikino sukuryuu |
JPS51138748A (en) * | 1975-05-28 | 1976-11-30 | Japan Steel Works Ltd | Device for mixing and melting plastic compound material |
JPS53129374A (en) * | 1977-04-18 | 1978-11-11 | Japan Steel Works Ltd:The | Double-shaft kneading and deairing extruder |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2002086542A (en) * | 2000-09-13 | 2002-03-26 | Tokyo Printing Ink Mfg Co Ltd | Extrusion molding method by twin-screw extruder |
JP4633240B2 (en) * | 2000-09-13 | 2011-02-16 | 東京インキ株式会社 | Extrusion molding method with twin screw extruder |
US10676603B2 (en) | 2015-07-16 | 2020-06-09 | The Japan Steel Works, Ltd. | Method for producing resin composition |
Also Published As
Publication number | Publication date |
---|---|
JPH021650B2 (en) | 1990-01-12 |
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