JPS607046B2 - Pulp particle manufacturing equipment - Google Patents

Pulp particle manufacturing equipment

Info

Publication number
JPS607046B2
JPS607046B2 JP15736575A JP15736575A JPS607046B2 JP S607046 B2 JPS607046 B2 JP S607046B2 JP 15736575 A JP15736575 A JP 15736575A JP 15736575 A JP15736575 A JP 15736575A JP S607046 B2 JPS607046 B2 JP S607046B2
Authority
JP
Japan
Prior art keywords
turbine
pipe
particles
stator
pulp
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
JP15736575A
Other languages
Japanese (ja)
Other versions
JPS5281110A (en
Inventor
勝彦 陶山
義治 伊藤
稔夫 辻
千嗣 北畠
清彦 山村
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.)
Unitika Ltd
Original Assignee
Unitika 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 Unitika Ltd filed Critical Unitika Ltd
Priority to JP15736575A priority Critical patent/JPS607046B2/en
Publication of JPS5281110A publication Critical patent/JPS5281110A/en
Publication of JPS607046B2 publication Critical patent/JPS607046B2/en
Expired legal-status Critical Current

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Description

【発明の詳細な説明】 本発明は、パルプ状粒子の製造装置に関するものであり
、さらに詳しくは、合成重合体溶液と沈殿剤溶液とを高
灘断力下で、接触させてパルプ状合成重合体粒子を製造
する装置に関するものである。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to an apparatus for producing pulp-like particles, and more specifically, a synthetic polymer solution and a precipitant solution are brought into contact with each other under high shear force to produce pulp-like synthetic polymer particles. The present invention relates to an apparatus for producing coalesced particles.

本発明にいうパルプ状粒子とは、繊維状あるいは薄葉状
の形状をもち、個々の粒子はそれぞれ同一の形状をもた
ない柔軟な微粒子であり、表面積が大きく、吸水能力の
高いもので、絡み合う能力が大きく該粒子単独のあるい
は短繊維と混合した水分散溶液より金網上に沈着させる
ことにより容易に紙状あるいはシート状物品を与えるも
のである。
The pulp-like particles referred to in the present invention are flexible fine particles that have a fibrous or thin leaf-like shape, each particle does not have the same shape, have a large surface area, have a high water absorption capacity, and are intertwined with each other. It has a large ability to easily produce paper-like or sheet-like articles by depositing the particles alone or in an aqueous dispersion solution mixed with short fibers on a wire mesh.

合成重合体溶液と沈殿剤溶液とを接触させて沈殿粒子を
形成させる場合、接触の際に両溶液にかかる鯉断力が該
粒子の形状に大きな影響を与える。
When a synthetic polymer solution and a precipitant solution are brought into contact to form precipitated particles, the shearing force applied to both solutions during contact has a large effect on the shape of the particles.

すなわち、両溶液にかかる数断力が大きい場合、沈殿粒
子は繊維状あるいは薄葉状のすりきれた形状をもち、逆
の場合は球状に近い形状をもつ。したがって、パルプ状
粒子を製造するためには、装置内に高敷断力のかかる領
域を設置するとともに両溶液を該高期断力領域へ導く手
段が必要となる。0 ところが、両溶液を接触させるこ
とにより形成されるパルプ状粒子を含む溶液は、粘糠で
あるとともにパルプ状固形物を含むため、該溶液の流動
方向が複雑に変化する装置では流動速度が減少しときに
は装置内でパルプ状粒子がつまり、流動不可能となるこ
とがある。
That is, when the number shear force applied to both solutions is large, the precipitated particles have a fibrous or thin leaf-like worn shape, and in the opposite case, they have a shape close to spherical. Therefore, in order to produce pulp-like particles, it is necessary to install a region in the apparatus where high shearing force is applied and to have a means for guiding both solutions to the high shearing force region. 0 However, the solution containing pulp-like particles formed by bringing both solutions into contact is viscous and contains pulp-like solids, so the flow rate decreases in devices where the flow direction of the solution changes in a complex manner. Sometimes, the pulp-like particles become clogged in the device, making it impossible to flow.

本発明者らは上記の問題点を解消すべく鋭意研究の結果
、パイプの内壁に空孔を有するステーターを固定し、該
ステーターにきわめて接近してタービンを高速に回転さ
せることにより、高灘断力領域となし、合成重合体溶液
および沈殿剤溶液の供給口をタービンの回転軸方向でタ
ービンの前方の近傍に設け、タービンの後方にパルプ状
粒子の排出口を設けることにより、該供給口から、両溶
液を導入して上記高酸断力領域でパルプ粒子を形成させ
たのち、ステーター内の空孔を経てステ−ターの後方に
ある排出口にほぼ直線的に溶液を導くことができ、装置
内での粒子のつまりを起こさずに連続的にパルプ状粒子
が製造しうろことを見出し、本発明に到達した。
As a result of intensive research in order to solve the above problems, the present inventors fixed a stator with holes on the inner wall of the pipe and rotated the turbine at high speed in close proximity to the stator. By providing a supply port for the synthetic polymer solution and a precipitant solution near the front of the turbine in the direction of the rotational axis of the turbine, and providing an outlet for pulp-like particles at the rear of the turbine, After both solutions are introduced and pulp particles are formed in the high acid shear region, the solution can be guided almost linearly through the holes in the stator to the outlet at the rear of the stator. The present invention was achieved by discovering that pulp-like particles can be produced continuously without clogging of the particles within the apparatus.

すなわち、本発明は、パイプ10中に、タービンを駆動
軸に固定するためのパイプ状部材と、該パイプ状部材の
先端にパイプの長さ方向と垂直に固定された円板と、該
円板上に固定され、タービン前方方向につき出た複数の
羽根状部村とよりなり、その回転軸がパイプの長さ方向
中心線上にあるタービン20と、これに接近して外鉄し
ており、パルプ状粒子分散溶液がタービン側から入って
タービン後方に通過できるようパイプの長さ方向に穿設
された1個以上の空孔を、前記羽根状部材の後方位置に
有するステーター30とが1対以上内臓してあり、かつ
該パイプの合成重合体溶液・沈殿剤溶液供給側にはター
ビン近傍の前方位置でタービンの駆動軸方向に開口した
合成重合体溶液の供給口41と、沈殿剤溶液の供給口4
2とを両液を同時に供給可能に配設し、タービンの後方
位置の排出側にはパルプ状粒子分散溶液の排出口45を
配設してなることを特徴とするパルプ状粒子の製造装置
である。
That is, the present invention includes, in the pipe 10, a pipe-like member for fixing the turbine to the drive shaft, a disc fixed to the tip of the pipe-like member perpendicularly to the length direction of the pipe, and the disc. The turbine 20 has a plurality of blade-shaped parts fixed to the upper part and protrudes toward the front of the turbine, and the rotation axis of the turbine 20 is on the center line in the length direction of the pipe. one or more pairs of stators 30 having one or more holes drilled in the length direction of the pipe at a rear position of the blade-like member so that the particle-dispersed solution can enter from the turbine side and pass to the rear of the turbine; On the synthetic polymer solution/precipitant solution supply side of the pipe, there is a synthetic polymer solution supply port 41 that opens in the direction of the turbine drive shaft at a forward position near the turbine, and a precipitant solution supply port 41. Mouth 4
2 and 2 are arranged so that both liquids can be supplied simultaneously, and an outlet 45 for the pulp-like particle dispersion solution is arranged on the discharge side at a rear position of the turbine. be.

本発明によるパルプ状粒子の製造装置の具体例を第1図
および第2図に示す。
A specific example of the apparatus for producing pulp-like particles according to the present invention is shown in FIGS. 1 and 2.

第1図は本発明の装置の長手方向の組立断面図であり、
第2図は第1図の1−1の線で切った断面図である。本
装置は、パイプ10、駆動軸1に固定されたタービン2
0パイプ10内に固定されたステーター30、全合成重
合体溶液供給口41、沈殿剤溶液供給口42およびパル
プ状粒子分散溶液排出口45とから主として構成されて
いる。さらに詳細に説明すると、パイプ1川さ、その−
2内径がステーター30の外径に等しい部分11と、該
外径より小さい部分12およびフランジ部13,14と
から構成されている。
FIG. 1 is a longitudinal assembled sectional view of the device of the present invention;
FIG. 2 is a sectional view taken along line 1--1 in FIG. This device includes a pipe 10 and a turbine 2 fixed to a drive shaft 1.
It is mainly composed of a stator 30 fixed in a pipe 10, a fully synthetic polymer solution supply port 41, a precipitant solution supply port 42, and a pulp-like particle dispersion solution discharge port 45. To explain in more detail, pipe 1 river, that-
The stator 30 is comprised of a portion 11 whose inner diameter is equal to the outer diameter of the stator 30, a portion 12 smaller than the outer diameter, and flange portions 13 and 14.

部分11の駆動軸方向の長さはステータ−30のそれと
一致し「 ここにステーター30を挿入し、フランジ部
13をフランジ部14に密着させることにより、ステー
タ−30の駆動軸方向の位置が固定される。またフラン
ジ部13にはピン状突起33がとり付けられ、これによ
りステー夕−30の駆動軸回転方向の位置が固定される
。フランジ13はパイプ内の乱流を防止するため、ター
ビン20の羽根状部材22の先端まで内壁19をのばし
てある。フランジ部13および14の接合面は平滑な面
でありo−リング17で密閉して、ボルト18およびフ
ランジ部14内にきったネジで接合される。タービン2
0‘ま、円板21、駆動軸1にタービン20を固定する
ためのパイプ状部材23および円板21上に固定された
羽根状部材22とから構成され、その回転軸がパイプ1
0の長さ方向中心線上にある。
The length of the portion 11 in the drive shaft direction matches that of the stator 30. By inserting the stator 30 here and bringing the flange portion 13 into close contact with the flange portion 14, the position of the stator 30 in the drive shaft direction is fixed. A pin-shaped protrusion 33 is attached to the flange portion 13, thereby fixing the position of the stator 30 in the rotational direction of the drive shaft. The inner wall 19 extends to the tip of the wing-like member 22 at 20. The joint surfaces of the flanges 13 and 14 are smooth surfaces and are sealed with an O-ring 17, and the bolts 18 and screws cut in the flange 14 are sealed. Turbine 2
0' is composed of a disk 21, a pipe-like member 23 for fixing the turbine 20 to the drive shaft 1, and a vane-like member 22 fixed on the disk 21, whose rotation axis is connected to the pipe 1.
0 on the longitudinal center line.

円板21はパイプ状部材23の先端にパイプ10の長さ
方向と垂直に固定されている。パイプ状部材23にはタ
ービン20を駆動軸1に固定するため、内部ネジが切っ
てあり、このネジによりタービン20とステ−夕−30
のあいだの間隔を接近させるようになっており、このま
しくはその間隔を2側以下に調整できるようになつてい
る。タービン20はこのようにステーター3川こきわめ
て接近して高速に回転するため、この間隙には高敷断力
が生じここに流入する合成重合体溶液と沈殿剤溶液とよ
りパルプ状粒子が形成される。タービン20の羽根状部
材22は、円板21上に固定され、タービン20の前方
方向につき出ているが、ステータ−ときわめて接近でき
る構造であれば、いかなる形状であってもよく、第1図
のごとく平面状あるいはこの平面をタービンの回転方向
に対して反対方向にねじったものあるいは半径方向に羽
根状部材の断面が増加するものなどがあげられる。
The disk 21 is fixed to the tip of the pipe-like member 23 perpendicularly to the length direction of the pipe 10. The pipe-shaped member 23 is internally threaded in order to fix the turbine 20 to the drive shaft 1, and this thread connects the turbine 20 and the stator 30.
The distance between the two sides is made closer, and preferably, the distance can be adjusted to two sides or less. Since the turbine 20 rotates at high speed in close proximity to the three stators, a high shearing force is generated in the gap, and pulp-like particles are formed by the synthetic polymer solution and precipitant solution flowing into the gap. Ru. The blade-like members 22 of the turbine 20 are fixed on the disc 21 and protrude toward the front of the turbine 20, but they may have any shape as long as they have a structure that allows them to be very close to the stator. Examples include a planar structure such as this, a planar structure twisted in the opposite direction to the rotational direction of the turbine, and a structure in which the cross section of the blade-like member increases in the radial direction.

また、羽根状部材22の枚数は流入する合成重合体溶液
と沈殿剤溶液とを高確率でタービン20とステ−夕‐3
0との間隙内に導くために少なくとも2枚以上であるこ
とが好ましい。ステーター301まパイプ10の長さ方
向に穿設された複数の空孔31を、羽根状部材22の後
方位置にもち「 タービン20とステーター30との間
隙で形成されたパルプ状粒子を含む溶液が、タービン2
0側からステーターの空孔31内に入り「 タービン2
0の後方に通過できる構造となっている。空孔の個数は
、1個以上であればいくらでもよく、また形状も円柱状
、惰円柱状等いかなる形状であってもよい。ただし、ス
テーター30を駆動軸1に垂直な方向に切断した際のス
テーター30の断面において空孔の占める面積が9.0
%Zをこえないことが好ましい。90%をこえると夕−
ビン20およびステーター30の間隙の高期断領域に入
れない沈殿剤溶液および合成重合体溶液量が増加するた
め、粗大な粒子が増加し、不均質なパルプ状粒子が形成
されるので好ましくない。
In addition, the number of blade-like members 22 is determined to ensure that the inflowing synthetic polymer solution and precipitant solution are transferred between the turbine 20 and the stator-3 with high probability.
It is preferable that the number of sheets be at least two or more in order to guide the sheet into the gap between the sheet and the sheet. The stator 301 has a plurality of holes 31 drilled in the length direction of the pipe 10 at a rear position of the blade-like member 22 so that a solution containing pulp-like particles formed in the gap between the turbine 20 and the stator 30 can be absorbed. , turbine 2
Enter into the air hole 31 of the stator from the 0 side and enter the turbine 2.
It has a structure that allows it to pass behind 0. The number of holes may be any number as long as it is one or more, and the shape may be any shape such as a cylindrical shape or a cylindrical shape. However, the area occupied by the holes in the cross section of the stator 30 when cut in the direction perpendicular to the drive shaft 1 is 9.0
It is preferable not to exceed %Z. When it exceeds 90%, it's evening.
Since the amount of the precipitant solution and the synthetic polymer solution that cannot enter the high-shutdown region of the gap between the bottle 20 and the stator 30 increases, the number of coarse particles increases and non-uniform pulp-like particles are formed, which is undesirable.

Z合成重合体の供給口41および沈殿剤溶液の供給口
42は、タービン20の駆動軸方向でタービン近傍の前
方に位置し、第1図のように沈殿剤溶液の導管43中に
合成重合体溶液の導管44を埋め込んだものが両溶液の
均一な混合上好ましいが、それぞれ異つた導管をタービ
ン20の直前まで導いた構造のものであってもよい。両
溶液の供給口41,42から、タービン20までの間で
は、両溶液が低酸断力下で接触するため、この供給口4
1,42からタービン20までの距離は好ましくは20
cの以下、さらに好ましくは10cm以下にするべきで
、20cの以上となると、形成された粒子中に球状に近
い粒子あるいは粗大な粒子が混入する傾向がある。
The supply port 41 for the Z synthetic polymer and the supply port 42 for the precipitant solution are located at the front near the turbine in the direction of the drive shaft of the turbine 20, and as shown in FIG. Although it is preferable to embed the solution conduit 44 in order to mix both solutions uniformly, it is also possible to have a structure in which different conduits are led to just before the turbine 20. Between the supply ports 41 and 42 of both solutions and the turbine 20, both solutions come into contact under a low acid shear force.
The distance from 1,42 to the turbine 20 is preferably 20
It should be less than c, more preferably 10 cm or less; if it is more than 20 cm, there is a tendency for near-spherical particles or coarse particles to be mixed into the formed particles.

パルプ状粒子の分散した溶液の排出口45は、タービン
20の後方に位置し、溶液が本装置内でほぼ直線的に流
動しうるようになっている。
An outlet 45 for the pulp-like particle dispersed solution is located at the rear of the turbine 20 so that the solution can flow approximately linearly within the device.

このため本装置は、流動抵抗が小さく、また、形成され
た粒子により装置内の一部がつまったりすることがなく
、生産速度の高いものとなる。1対のタービン20とス
テーター30のみでは奥断力が不足であったり、形成さ
れたパルプ状粒子が粗大なため、さらに摩り潰す必要が
ある場合には1対以上のタービンとステーターを運転す
ることも可能である。
Therefore, the present apparatus has a low flow resistance, prevents part of the apparatus from becoming clogged with formed particles, and has a high production rate. If only one pair of turbine 20 and stator 30 is insufficient to provide sufficient cutting force, or the formed pulp particles are coarse, and it is necessary to grind them further, one or more pairs of turbine and stator should be operated. is also possible.

また、この製造装置にポンプ的能力を付与せしめるため
のタービンおよびステーターを連結してもよい。本装置
は、駆動軸1および同軸上に固定されたタービン20を
、高速で回転させつつ、合成重合体溶液を供給口41よ
り、沈殿剤溶液を供給口42より圧送し「両溶液をター
ビン20およびステーター30との間隙の高敷断力領域
を通過させ、形成されたバルブ状粒子の分散した溶液を
ステー夕−30内の空孔31を通過させ、排出口45か
らとり出すことにより作動させることができる。
Further, a turbine and a stator may be connected to provide pumping ability to this manufacturing apparatus. This device rotates a drive shaft 1 and a turbine 20 fixed on the same axis at high speed, and pumps a synthetic polymer solution through a supply port 41 and a precipitant solution through a supply port 42. and the stator 30, and the solution in which the formed bulb-shaped particles are dispersed passes through the holes 31 in the stator 30 and is taken out from the discharge port 45 to operate. be able to.

以下に本装置の作動試験の一例をあげる。ポリメタフェ
ニレンイソフタルアミド14重量%、塩化カルシウム4
重量%、N,N一ジメチルアセトアミド82重量%から
なる重合体溶液を、毎分1.5その割合で供給口41よ
り、また沈殿剤としてグリセリンを毎分47その割合で
供給口42より360仇pmで回転しているタービン2
0およびステーター30の領域に圧送して、パルプ状粒
子を含む分散溶液を排出口45より毎分約48.5その
割合でとり出した。
Below is an example of an operation test of this device. Polymetaphenylene isophthalamide 14% by weight, calcium chloride 4%
A polymer solution consisting of 82% by weight of N,N-dimethylacetamide was fed through the supply port 41 at a rate of 1.5% per minute, and glycerin as a precipitant was fed at a rate of 47% per minute from the supply port 42 at a rate of 360% by weight. Turbine 2 rotating at pm
0 and the stator 30, and a dispersion solution containing pulp-like particles was taken out from the outlet 45 at a rate of about 48.5 per minute.

とり出した分散溶液を櫨過後、水洗して精製パルプ状粒
子を得た。得られた粒子は、ポリメタフェニレンィソフ
タルアミドの短繊維と混合して水中に分散させ、金網上
で沈着させることにより容易に紙状物質を与えるもので
あった。
The taken out dispersion solution was filtered through a filter and washed with water to obtain purified pulp-like particles. The obtained particles could easily be mixed with short fibers of polymetaphenylene isophthalamide, dispersed in water, and deposited on a wire mesh to give a paper-like material.

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

0 第1図は本発明の装置の長手方向の組立断面図であ
り、第2図は第1図の1−1の線で切った断面図である
。 1・・・・・・駆動軸、10…・・・パイプ、20…・
・・タービン、30…・・・ステーター「 41・・・
・・・合成重合体5溶液供給口「 42・・・…沈殿剤
溶液供給口、45……排出口。 矛‘図 希2図
0 FIG. 1 is a longitudinal assembled sectional view of the device of the present invention, and FIG. 2 is a sectional view taken along the line 1--1 in FIG. 1... Drive shaft, 10... Pipe, 20...
...Turbine, 30...Stator "41...
...Synthetic polymer 5 solution supply port 42...Precipitant solution supply port, 45...Discharge port.

Claims (1)

【特許請求の範囲】[Claims] 1 パイプ10中に、タービンを駆動軸に固定するため
のパイプ状部材と、該パイプ状部材の先端にパイプの長
さ方向と垂直に固定された円板と、該円板上に固定され
、タービン前方方向につき出た複数の羽根状部材とより
なり、その回転軸がパイプの長さ方向中心線上にあるタ
ービン20と、これに接近して外嵌しており、パルプ状
粒子分散溶液がタービン側から入ってタービン後方に通
過できるようにパイプの長さ方向に穿設された1個以上
の空孔を、前記羽根状部材の後方位置に有するステータ
ー30とが1対以上内臓してあり、かつ該パイプの合成
重合体溶液・沈殿剤溶液供給側にはタービン近傍の前方
位置でタービンの駆動軸方向に開口した合成重合体溶液
の供給口41と、沈殿剤溶液の供給口42とを両液を同
時に供給可能に配設し、タービンの後方位置の排出側に
はパルプ状粒子分散液の排出口45を配設してなること
を特徴とするパルプ状粒子の製造装置。
1. In the pipe 10, a pipe-like member for fixing the turbine to the drive shaft, a disc fixed at the tip of the pipe-like member perpendicular to the length direction of the pipe, and fixed on the disc, The turbine 20 is made up of a plurality of blade-like members protruding toward the front of the turbine, and its rotation axis is on the center line in the longitudinal direction of the pipe. One or more pairs of stators 30 are built in, the stator 30 having one or more holes bored in the length direction of the pipe at a rear position of the blade-like member so that the pipe can enter from the side and pass behind the turbine, In addition, on the synthetic polymer solution/precipitant solution supply side of the pipe, a synthetic polymer solution supply port 41 and a precipitant solution supply port 42, which are open in the direction of the turbine drive shaft at a forward position near the turbine, are provided. A device for producing pulp-like particles, characterized in that the liquid is arranged so that liquids can be supplied simultaneously, and a discharge port 45 for a pulp-like particle dispersion liquid is arranged on the discharge side at a rear position of the turbine.
JP15736575A 1975-12-25 1975-12-25 Pulp particle manufacturing equipment Expired JPS607046B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP15736575A JPS607046B2 (en) 1975-12-25 1975-12-25 Pulp particle manufacturing equipment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP15736575A JPS607046B2 (en) 1975-12-25 1975-12-25 Pulp particle manufacturing equipment

Publications (2)

Publication Number Publication Date
JPS5281110A JPS5281110A (en) 1977-07-07
JPS607046B2 true JPS607046B2 (en) 1985-02-22

Family

ID=15648055

Family Applications (1)

Application Number Title Priority Date Filing Date
JP15736575A Expired JPS607046B2 (en) 1975-12-25 1975-12-25 Pulp particle manufacturing equipment

Country Status (1)

Country Link
JP (1) JPS607046B2 (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP5076424B2 (en) * 2006-09-28 2012-11-21 日油株式会社 Stir processing method and stirrer

Also Published As

Publication number Publication date
JPS5281110A (en) 1977-07-07

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