JPS5829725B2 - Polymer no. - Google Patents

Polymer no.

Info

Publication number
JPS5829725B2
JPS5829725B2 JP50147662A JP14766275A JPS5829725B2 JP S5829725 B2 JPS5829725 B2 JP S5829725B2 JP 50147662 A JP50147662 A JP 50147662A JP 14766275 A JP14766275 A JP 14766275A JP S5829725 B2 JPS5829725 B2 JP S5829725B2
Authority
JP
Japan
Prior art keywords
polymer
mixing
polymers
rotating shaft
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.)
Expired
Application number
JP50147662A
Other languages
Japanese (ja)
Other versions
JPS5269962A (en
Inventor
成雄 安斎
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.)
Kuraray Co Ltd
Original Assignee
Kuraray Co Ltd
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 Kuraray Co Ltd filed Critical Kuraray Co Ltd
Priority to JP50147662A priority Critical patent/JPS5829725B2/en
Publication of JPS5269962A publication Critical patent/JPS5269962A/en
Publication of JPS5829725B2 publication Critical patent/JPS5829725B2/en
Expired legal-status Critical Current

Links

Description

【発明の詳細な説明】 本発明は、ポリマーの複合混合方法および混合装置に関
する。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method and apparatus for complex mixing of polymers.

一般に合成繊維等の改良のため数バーセントル数10パ
ーセントの異種ポリマーを混合することが行なわれるが
、従来非スタテック(動的)混合方法装置としてはチッ
プブレンド、あるいは異種ポリマー液でのスクリュー等
による混合が行なわれている。
In order to improve synthetic fibers, it is generally done to mix several tens of percent of different polymers, but conventional non-static (dynamic) mixing methods include chip blending, mixing with different polymer liquids using screws, etc. is being carried out.

しかし、かかる従来装置、方法による場合、ポリマーの
場合はスクリューまたは攪拌翼での回転せん断による混
合であるため、混合状態が不完全、不均一であり、均一
な混合相に於いては各成分相が微細に成りすぎるため、
粗にしてかつ均一化された混合相ポリマーを得ることは
非常に困難であった。
However, when using such conventional equipment and methods, polymers are mixed by rotating shear using a screw or stirring blade, so the mixing state is incomplete and non-uniform, and each component phase is different from a uniform mixed phase. becomes too fine,
It has been very difficult to obtain coarse and homogenized mixed phase polymers.

本発明は、かかる従来の欠点を解消するためになされた
もので、シリンダー状混合槽内に多数の小孔群を有する
回転体を装置したもので、回転体内部の小孔群からポリ
マーAを回転体外部へ供給されたポリマーBの中へ放射
線状に射出し、このポリマーA、Bの回合部に複合相を
形成し、かつ回転により適度に複合混合させることを特
徴とするものである。
The present invention has been made to eliminate such conventional drawbacks, and includes a rotating body having a large number of small holes in a cylindrical mixing tank, and polymer A is extracted from the small holes inside the rotating body. This is characterized by radially injecting the polymer B into the polymer B supplied to the outside of the rotating body, forming a composite phase at the combined part of the polymers A and B, and mixing the composite appropriately by rotation.

以下本発明の実施例を図面により説明する。Embodiments of the present invention will be described below with reference to the drawings.

Aは少なくとも1種のポリマー成分よりなるポリマーA
、Bは少なくとも1種のポリマー成分よりなるAポリマ
ーと異なるポリマーBを示す。
A is a polymer A consisting of at least one polymer component
, B indicates a polymer B that is different from the A polymer and is composed of at least one polymer component.

1は混合シリンダー(混合槽)であり、1方にポリマー
A、Bの供給口2A、2Bを有し、他端に口金装置等1
1に通ずる複合混合ポリマーの出口通路10を有してい
る筒状体である。
1 is a mixing cylinder (mixing tank), which has supply ports 2A and 2B for polymers A and B on one end, and a cap device 1 on the other end.
1 is a cylindrical body having an outlet passageway 10 of the composite mixed polymer leading to the cylindrical body 1 .

3は回転軸で中空構造でシリンダー1の供給口2Aに対
応した位置に中空部ヘポリマーAを導入するためのポリ
マー用溝4Aおよびポリマースリット5Aを有し、また
供給口2Bに対応してシリンダー1との間にポリマーB
用の溝4B、およびポリマースリット5Bを形成してい
る。
Reference numeral 3 denotes a rotating shaft having a hollow structure and having a polymer groove 4A and a polymer slit 5A for introducing polymer A into the hollow portion at a position corresponding to the supply port 2A of the cylinder 1, and a shaft 3 corresponding to the supply port 2B of the cylinder 1. Polymer B between
grooves 4B and polymer slits 5B.

また、射出方向に向って回転軸3の中空部6よりシリン
ダー1との複合混合空間9に向って放射線状に多数の小
孔部7を有したものである。
Further, it has a large number of small holes 7 radially extending from the hollow part 6 of the rotating shaft 3 toward the composite mixing space 9 with the cylinder 1 in the injection direction.

なお、ポリマーAの供給口2人は必ずしもシリンダーI
VC設げられていなくても良く、回転軸3に設けられた
流入路2A’でも良い。
Note that the two supply ports for Polymer A are not necessarily connected to Cylinder I.
It is not necessary to provide a VC, and the inflow path 2A' provided on the rotating shaft 3 may be used.

8はポリマーA、Bが混合しないためのポリマー溝4A
、4B間での軸シールである。
8 is a polymer groove 4A for preventing polymers A and B from mixing.
, 4B is the shaft seal.

12はシリンダー1と回転軸3との軸シールである。12 is a shaft seal between the cylinder 1 and the rotating shaft 3.

本発明装置に於いて、ポリマーAは供給口2Aかも供給
され、溝4Aからスリン)5Aを通り中空部6に至り、
lJ寸し群7より射出され空間9に存するポリマーBと
の間に複合混合される。
In the device of the present invention, polymer A is also supplied from the supply port 2A, passes through the groove 4A through the sulin 5A, and reaches the hollow part 6.
The polymer B is injected from the lJ size group 7 and mixed with the polymer B present in the space 9.

また、ポリマーBは供給口2Bより供給溝4Bへ流入し
、スリット5Bよりシリンダー外周より均一に空間9へ
送り出されるのである。
Further, the polymer B flows into the supply groove 4B from the supply port 2B, and is uniformly sent out from the outer circumference of the cylinder to the space 9 through the slit 5B.

そしてこの複合混合空間9に於いて、本発明の特徴であ
る混合複合が行なわれる。
In this composite mixing space 9, mixing and composite, which is a feature of the present invention, is performed.

すなわち、該空間9に流れるポリマーBに対して、ポリ
マーAは小孔群より島状に複合する如く射出される。
That is, with respect to the polymer B flowing into the space 9, the polymer A is injected from the small pores so as to form a composite island.

模式的には第2図の説明図のように示される。It is schematically shown as an explanatory diagram in FIG.

図2−1は複合状態を直線的に模示しており、さらにこ
れに図2−2に示すごとく軸の回転によるラセン状引き
のばし作用が回転作用により任意に加わり、ポリマーA
Bの混合は連続的かつ均一に複合混合が進むのである。
Figure 2-1 shows a linear representation of the composite state, and as shown in Figure 2-2, a helical stretching action due to the rotation of the shaft is optionally added to this by the rotation action, and polymer A
In the mixing of B, complex mixing progresses continuously and uniformly.

かかる混合ポリマーは、適度にして均一な混合相を有す
るのであり、改良された繊維等の製造を可能にするので
ある。
Such mixed polymers have a moderately uniform mixed phase and enable the production of improved fibers and the like.

また、本装置方法に於いて、ポリマーAの流入口2Aは
必ずしも例図の如くシリンダー1に設けられていなくて
も良く、回転軸3に破線で示した流入路2N等でも同じ
効果が得られろ。
In addition, in this apparatus method, the polymer A inlet 2A does not necessarily need to be provided in the cylinder 1 as shown in the example diagram, and the same effect can be obtained by using the inlet channel 2N shown by the broken line on the rotating shaft 3. reactor.

シリンダー1の空間形状は、通常ストレート円筒形であ
るが、目的の複合混合形態を得るために第3図の3−1
図の如き形状もとりうるし、3−2図の如きテーパー形
状でも良いのである。
The space shape of the cylinder 1 is normally a straight cylinder, but in order to obtain the desired composite mixing form, the space shape is changed to 3-1 in Figure 3.
It may have a shape as shown in the figure, or it may have a tapered shape as shown in Figure 3-2.

また、回転軸形状についても、第4図に例示のごとく任
意の形状が選定できる。
Further, as for the shape of the rotating shaft, any shape can be selected as illustrated in FIG. 4.

さらに、回転軸に設けられた孔径、孔数および配列は、
ポリマーの粘度や回転数シリンダーとの位置関係等に合
わせて適宜変えることもできる。
Furthermore, the diameter, number and arrangement of holes provided on the rotating shaft are as follows:
It can also be changed as appropriate depending on the viscosity of the polymer, the rotation speed, and the positional relationship with the cylinder.

以上の如き本発明装置に於いて、複合混合繊維を紡糸す
れば良好な紡糸調子で繊維の谷部に適度に粗で且つ均一
な混合相を有する優れた繊維が得られるのである。
When the composite mixed fiber is spun using the apparatus of the present invention as described above, an excellent fiber having a suitably coarse and uniform mixed phase in the fiber troughs can be obtained with good spinning conditions.

本発明に用いられるポリマーA、Bは、ナイロン、ポリ
エチレン、ポリエチVンテンフタレートポリ塩化ビニル
等公知の合成高分子物質が使用できろ。
As the polymers A and B used in the present invention, known synthetic polymer materials such as nylon, polyethylene, and polyvinyl chloride may be used.

また、ポリマーA1ポリマーBは通常は異物質であるが
、必ずしも異物質であることは必要ではなく、類似の高
分子物質の混合であってもよい。
Further, although polymer A and polymer B are usually different substances, they do not necessarily need to be different substances, and may be a mixture of similar polymer substances.

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

第1図は本発明の代表的装置例である。 第2図は本発明方法による複合混合の説明図であり、第
3図、第4図はシリンダーおよび回転軸の例図である。
FIG. 1 shows a typical example of the device of the present invention. FIG. 2 is an explanatory diagram of complex mixing according to the method of the present invention, and FIGS. 3 and 4 are examples of a cylinder and a rotating shaft.

Claims (1)

【特許請求の範囲】 12種以上のポリマーの動的複合混合に際し、ポリマー
Bを回転型混合装置の回転軸外部から円周軸方向に供給
し、ポリマーAを回転軸内部のポリマー流路から外部に
向って放射線状に設けられた小孔群から該軸外部へ射出
し、前記ポリマーAと混合することを特徴とするポリマ
ーの動的複合混合方法。 2 回転型混合装置に於いて、回転軸が少なくとも1個
の流入口を有し、他端に多数の射出孔群を有する筒状物
であり、該筒状物の外面は任意の空間をもって混合シリ
ンダー(混合槽)によって囲まれていることを特徴とす
るポリマーの動的複合混合装置。
[Claims] In dynamic composite mixing of 12 or more polymers, polymer B is supplied circumferentially from the outside of the rotating shaft of a rotary mixing device, and polymer A is supplied from the polymer flow path inside the rotating shaft to the outside. 1. A method for dynamic composite mixing of polymers, characterized in that the polymer is injected to the outside of the shaft from a group of small holes provided radially toward the shaft and mixed with the polymer A. 2 In a rotary mixing device, the rotating shaft is a cylindrical body having at least one inlet and a large number of injection holes at the other end, and the outer surface of the cylindrical body has an arbitrary space for mixing. A dynamic composite mixing device for polymers, characterized in that it is surrounded by a cylinder (mixing tank).
JP50147662A 1975-12-10 1975-12-10 Polymer no. Expired JPS5829725B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP50147662A JPS5829725B2 (en) 1975-12-10 1975-12-10 Polymer no.

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP50147662A JPS5829725B2 (en) 1975-12-10 1975-12-10 Polymer no.

Publications (2)

Publication Number Publication Date
JPS5269962A JPS5269962A (en) 1977-06-10
JPS5829725B2 true JPS5829725B2 (en) 1983-06-24

Family

ID=15435422

Family Applications (1)

Application Number Title Priority Date Filing Date
JP50147662A Expired JPS5829725B2 (en) 1975-12-10 1975-12-10 Polymer no.

Country Status (1)

Country Link
JP (1) JPS5829725B2 (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS61154772U (en) * 1985-03-16 1986-09-25
CN104645844A (en) * 2011-03-15 2015-05-27 中国纺织科学研究院 Dynamic mixer

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP1669131A1 (en) * 2004-12-13 2006-06-14 Sika Technology AG Dynamic mixer
DE102014004862A1 (en) * 2014-04-03 2015-10-08 Dürr Systems GmbH Mixer and corresponding operating procedure
CN112045883B (en) * 2020-08-28 2022-09-09 东莞市信诚硅胶电子有限公司 Novel plasticator of rubber can overturn automatically

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS61154772U (en) * 1985-03-16 1986-09-25
CN104645844A (en) * 2011-03-15 2015-05-27 中国纺织科学研究院 Dynamic mixer

Also Published As

Publication number Publication date
JPS5269962A (en) 1977-06-10

Similar Documents

Publication Publication Date Title
US3209402A (en) Apparatus for producing multicom-ponent filaments and yarns
DE60010128T2 (en) DEVICE AND METHOD FOR SPINNING MATERIALS
US2440761A (en) Apparatus for producing artificial filaments
US3293117A (en) High density pulp mixing
SE445052C (en) SET AND DEVICE FOR CONTINUOUS MIXING OF GAS AND / OR LIQUID TREATMENTS IN A MASSAGE SUSPENSION
GB1466140A (en) Antistatic polyester filaments
DE2506258A1 (en) COLORED YARN AND THE PROCESS AND SPIDER DESIGN FOR THE MANUFACTURE OF THESE
JP2000328345A (en) Apparatus for coloring spinning raw material
JPS5829725B2 (en) Polymer no.
US3911073A (en) Process for inverting flow in a conduit
US4319848A (en) Apparatus for the production of additive containing synthetic linear polymers
DE69736361T2 (en) Formation of a solution of fluids with low miscibility and great difference in viscosity
DE4220239A1 (en) Mixer for inter-reacting liquid and gaseous ingredients - to produce homogeneous and stable product which flows steadily
GB983638A (en) Method and apparatus for spinning artificial filaments
US4474545A (en) Device for manufacturing multicolored marble soaps, from a base paste and one or more liquid pigments
DE872770C (en) Thrust centrifugal machine
EP1288349B1 (en) Apparatus for melt spinning and cooling of bundles of filaments
CN1072971A (en) The processing method of spray nozzle device and yarn
US2796240A (en) Dual pump
US3802668A (en) Apparatus for inverting flow in a conduit
US2961223A (en) Additive injecting and blending apparatus for filament spinning
US3273200A (en) Distributor plate
DE2350529A1 (en) SPINNING CHAMBER FOR SPINDLELESS SPINNING
JPH02307518A (en) Fluid mixing apparatus
CN207654973U (en) A kind of polyurethane blender agitating device