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JPS5939382B2 - Method for reinforcing inorganic fibers - Google Patents
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JPS5939382B2 - Method for reinforcing inorganic fibers - Google Patents

Method for reinforcing inorganic fibers

Info

Publication number
JPS5939382B2
JPS5939382B2 JP51098041A JP9804176A JPS5939382B2 JP S5939382 B2 JPS5939382 B2 JP S5939382B2 JP 51098041 A JP51098041 A JP 51098041A JP 9804176 A JP9804176 A JP 9804176A JP S5939382 B2 JPS5939382 B2 JP S5939382B2
Authority
JP
Japan
Prior art keywords
inorganic fibers
surface treatment
fibers
water vapor
treatment tank
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
JP51098041A
Other languages
Japanese (ja)
Other versions
JPS5324425A (en
Inventor
正 佐藤
繁量 草薙
次郎 伊藤
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.)
Panasonic Electric Works Co Ltd
Original Assignee
Matsushita Electric Works 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 Matsushita Electric Works Ltd filed Critical Matsushita Electric Works Ltd
Priority to JP51098041A priority Critical patent/JPS5939382B2/en
Publication of JPS5324425A publication Critical patent/JPS5324425A/en
Publication of JPS5939382B2 publication Critical patent/JPS5939382B2/en
Expired legal-status Critical Current

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  • Surface Treatment Of Glass Fibres Or Filaments (AREA)
  • Treatments For Attaching Organic Compounds To Fibrous Goods (AREA)

Description

【発明の詳細な説明】 本発明は製綿直後の無機質繊維5を表面処理槽−1内に
送入し一般式がT i (0R)4 (R= C4桟。
DETAILED DESCRIPTION OF THE INVENTION In the present invention, inorganic fibers 5 immediately after cotton production are fed into a surface treatment tank 1, and the general formula is T i (0R)4 (R=C4 crosspiece).

C3H7、C2H5]であられされる有機チタン化合物
の処理蒸気19と水蒸気18とをこの無機質繊維5に連
続的に接触させると共に無機質繊維5の移送方向に対す
る上記水蒸気18と処理蒸気19との濃度比に勾配をも
たせることを特徴とする無機質繊維の強化方法に係り、
その目的とするところは無機質繊維の保護皮膜による強
化を一層確実に行ない得る無機質繊維の強化方法を提供
するにある。
C3H7, C2H5] The organic titanium compound treated vapor 19 and the water vapor 18 are brought into continuous contact with the inorganic fibers 5, and the concentration ratio of the above water vapor 18 and the treated vapor 19 with respect to the direction of transport of the inorganic fibers 5 is adjusted. Relating to a method for reinforcing inorganic fibers characterized by providing a gradient,
The purpose is to provide a method for reinforcing inorganic fibers that can more reliably strengthen the inorganic fibers with a protective film.

一般にガラスウール、ロックウール等の無機質繊維は溶
融紡糸後の機械的、化学的な表面損傷がなければ非常に
大きな引張強度(200〜300kg/my?t )を
有する。
Generally, inorganic fibers such as glass wool and rock wool have a very high tensile strength (200 to 300 kg/my?t) unless there is mechanical or chemical surface damage after melt spinning.

この機械的、化学的な表面損傷を避けるために例えばガ
ラス長繊維に関しては、サイジング剤と称して各種樹脂
被膜が繊維表面に均一に施されている。
In order to avoid this mechanical and chemical surface damage, for example, with respect to long glass fibers, various resin coatings called sizing agents are uniformly applied to the fiber surfaces.

しかしながらガラスウール、ロックウール等の無機質繊
維は円盤法、高速気流吹付法によって大量に製綿される
ため、製綿時の表面処理はバインダのスプレー程度であ
り、繊維表面に均一な被膜を形成することができず、部
分的に液滴が付着している状態であった。
However, since inorganic fibers such as glass wool and rock wool are made in large quantities by the disc method or high-speed air blowing method, the surface treatment during cotton production is limited to a binder spray, which forms a uniform film on the fiber surface. It was not possible to do so, and droplets were partially attached.

このためにたとえ表面処理を施してもウール状ガラス質
短繊維は製綿後の機械的接触により著しく劣化していた
For this reason, even after surface treatment, wool-like short glass fibers were significantly degraded by mechanical contact after cotton-making.

このような事情に鑑みてウール状ガラス質短繊維の表面
に均一な保護皮膜を形成し、初期強度を保持する目的で
製綿直後、表面処理剤を蒸気状で吹付けて高温の繊維表
面で熱分解等の化学反応を起こさせる方法が検討されつ
つあるが、繊維表面に付着した皮膜の均一性、膜厚等が
未だ充分でないために満足な結果が得られていないのが
現状である。
In view of these circumstances, in order to form a uniform protective film on the surface of wool-like glass short fibers and maintain their initial strength, a surface treatment agent is sprayed in vapor form immediately after cotton production to coat the fiber surface at high temperature. Methods of causing chemical reactions such as thermal decomposition are being considered, but at present, satisfactory results have not been obtained because the uniformity and thickness of the film attached to the fiber surface are still insufficient.

また一般にガラスウール、ロックウール等の無機質短繊
維は1300〜1500℃の高温で溶融された鉱物原料
を高速回転する円盤上に導き、その遠心力によって円盤
の周囲から繊維化するか或いはノズルから噴出された高
速気流又は火炎で吹飛ばせて繊維化する。
Generally, inorganic short fibers such as glass wool and rock wool are produced by introducing mineral raw materials melted at a high temperature of 1,300 to 1,500 degrees Celsius onto a disk rotating at high speed, and the centrifugal force of the fibers forming the fibers from around the disk or ejecting them from a nozzle. It is blown away by high-speed airflow or flame and turned into fibers.

これらの繊維は輸送用気流によって集綿箱に送り込まれ
コンベアネットコンベアベルト等の上に集積されて搬送
される。
These fibers are fed into a collection box by the transport air current, collected on a conveyor net conveyor belt, etc., and transported.

本発明は集綿時、即ちコンベアネット(ベルト)上にゆ
るく(ルーズに)堆積した製綿直後の無機質繊維に有機
チタン化合物を処理するもので、以下添付図に基づいて
詳細に説明する。
The present invention treats inorganic fibers that are loosely deposited on a conveyor net (belt) immediately after cotton production with an organic titanium compound during cotton collection, and will be described in detail below with reference to the accompanying drawings.

まず上記製綿直後の無機質繊維5をそのままの状態で(
太きな外的な力を加えることなしに)表面処理槽1中に
連続的に搬入する。
First, the above-mentioned inorganic fiber 5 immediately after cotton-making is left as it is (
(without applying a large external force) into the surface treatment tank 1.

第1図は本発明に係る処理方法に使用する装置の一実施
例の概略を例示したものであって、1は円筒形の表面処
理槽であり、その内部にはガイド翼2を螺旋状に設けで
ある。
FIG. 1 schematically illustrates an embodiment of the apparatus used in the treatment method according to the present invention, in which 1 is a cylindrical surface treatment tank, inside which guide blades 2 are spirally arranged. It is a provision.

ガイド翼2の中心部には円孔状の欠損部3が設けられ、
かつ中心軸に沿って処理蒸気の導入管4を挿入配設しで
ある。
A hole-shaped defect 3 is provided in the center of the guide blade 2,
A processing steam introduction pipe 4 is inserted along the central axis.

6は処理蒸気19を含有した加熱空気の吐出ノズルであ
り、導入管4上に適描間隔をおいて設けである。
Reference numeral 6 indicates a discharge nozzle for discharging heated air containing processing steam 19, which is provided on the introduction pipe 4 at appropriate intervals.

その個数は特に限定しない。The number is not particularly limited.

7は表面処理槽1のガイド外筒であり、その内部にはス
チーム8を導入し、処理温度に処理槽内温を保つように
配慮しである。
Reference numeral 7 denotes a guide outer cylinder of the surface treatment tank 1, into which steam 8 is introduced to maintain the internal temperature of the treatment tank at the treatment temperature.

9は水蒸気18を含有した加熱空気の導入管、10は排
気管である。
9 is an introduction pipe for heated air containing water vapor 18, and 10 is an exhaust pipe.

lL12は表面処理槽1壁の該当箇所を多孔状になした
部分であり、加熱空気の導入排気が可能なように加工し
である。
1L12 is a porous portion of the wall of the surface treatment tank 1, which is processed to allow heated air to be introduced and exhausted.

13は伝動軸であり、電動機(図中に示さず)に連結し
である。
13 is a transmission shaft, which is connected to an electric motor (not shown in the figure).

14は軸受け、15は軸受けの支持アーム、16゜17
はそれぞれ搬送用のコンベアである。
14 is the bearing, 15 is the support arm of the bearing, 16° 17
are conveyors for transportation.

しかして製綿後、搬送用のコンベア16上にルーズに堆
積されたウール状の無機質繊維5を表面処理槽1内に連
続的に送り込む。
After cotton-making, the wool-like inorganic fibers 5 loosely deposited on the conveyor 16 are continuously fed into the surface treatment tank 1.

表面処理槽1は伝動軸13によって回転運動をなし、ガ
イド翼2によって無機質繊維5はゆっくりと表面処理槽
1内を移動する。
The surface treatment tank 1 is rotated by a transmission shaft 13, and the inorganic fibers 5 are slowly moved within the surface treatment tank 1 by the guide blades 2.

また導入管9より水蒸気18を含有した加熱空気を表面
処理槽1内に導入し無機質繊維5の移行と向流に流動せ
しめて排気管10より排気せしめる。
Further, heated air containing water vapor 18 is introduced into the surface treatment tank 1 through the introduction pipe 9, flowed in a countercurrent to the transfer of the inorganic fibers 5, and exhausted through the exhaust pipe 10.

更に有機チタン化合物T i (0R)4(R−=C4
’Hg、C3H72C2H5]の処理蒸気19を含有し
た加熱空気を吐出ノズル6より噴出させる。
Furthermore, an organic titanium compound T i (0R)4(R-=C4
Heated air containing treated steam 19 of 'Hg, C3H72C2H5] is ejected from the discharge nozzle 6.

上記有機チタン化合物の処理蒸気19と水蒸気18とは
雰囲気温度、それぞれの濃度、更には両者の濃度比等に
よって無機質繊維5の表面に複雑な無定形チタン化合物
皮膜を形成する。
The organic titanium compound treatment vapor 19 and the water vapor 18 form a complex amorphous titanium compound film on the surface of the inorganic fiber 5 depending on the ambient temperature, their respective concentrations, and their concentration ratio.

かかる処理に伴なう表面処理槽1内の濃度分布の有様を
示したのが第2図であり、水蒸気濃度は導入位置Aに於
いて最も高く、順次消費されて排気位置Bにおいて最も
希薄となる。
Figure 2 shows the concentration distribution in the surface treatment tank 1 accompanying such treatment, where the water vapor concentration is highest at the introduction position A, and is sequentially consumed until it is the most diluted at the exhaust position B. becomes.

一方処理蒸気濃度は表面処理槽1内で均等に吐出されて
いるが、消費されない余剰蒸気が、水蒸気を含んだ加熱
空気によって無機質繊維5の搬入口の方向に押し流され
るため、水蒸気とは逆にB位置が最も高く、A位置が最
も低くなる傾向がある。
On the other hand, the concentration of the treated steam is uniformly discharged in the surface treatment tank 1, but the surplus steam that is not consumed is pushed away by the heated air containing water vapor in the direction of the inlet of the inorganic fiber 5. The B position tends to be the highest and the A position the lowest.

他方第3図は濃度比(H20/T i (0R)4]と
皮膜性質のうち硬度と耐アルカリ性について示したもの
で、第2図より分るように搬入口から搬出口に至る迄濃
度比は次第に高くなり、第3図に示す如く表面処理槽内
の位置によって生成される皮膜の性質が異なってくる。
On the other hand, Figure 3 shows the concentration ratio (H20/T i (0R)4) and the hardness and alkali resistance of the film properties. gradually increases, and as shown in FIG. 3, the properties of the film produced differ depending on the position within the surface treatment tank.

本発明の処理方法の特徴は上記の点に存し、繊維表面に
形成された皮膜の性質が厚さ方向に異なり、上記の例で
は繊維表面に近い部分は耐アルカリ性が非常に良好であ
り、表面に近い部分は硬度が高い皮膜となる。
The characteristics of the treatment method of the present invention reside in the above points, and the properties of the film formed on the fiber surface differ in the thickness direction, and in the above example, the part close to the fiber surface has very good alkali resistance. The part near the surface becomes a hard film.

尚、有機チタン化合物T i (QC4桟)4 、Ti
(OCaH7)+ 、Ti(OC2H5)4を用いて無
機質繊維の表面処理を行なうにあたっては、各化合物の
いずれにおいても一般的にキャリアガスとしてN2を用
い、有機チタン化合物の蒸気濃度1000〜2500p
pm1流量50〜3ool/分、温度200〜350℃
、水蒸気の濃度1000〜5000ppm1流量50〜
3001/分、温度200〜350℃、処理時間1〜5
分の範囲内において各化合物とも同様な条件下で表面処
理を行なうことができる。
In addition, organic titanium compound T i (QC4 crosspiece) 4, Ti
When performing surface treatment on inorganic fibers using (OCaH7)+ and Ti(OC2H5)4, N2 is generally used as a carrier gas for each compound, and the vapor concentration of the organic titanium compound is 1000 to 2500 p.
pm1 flow rate 50-3oool/min, temperature 200-350℃
, water vapor concentration 1000~5000ppm1 flow rate 50~
3001/min, temperature 200-350℃, processing time 1-5
The surface treatment can be carried out under similar conditions for each compound within a range of 10 minutes.

本発明にあっては上述のように製綿直後の無機質繊維を
表面処理槽内に送入し一般式がT 1(OR)4〔R二
C4H9,C3H7,C2H5〕であられされる有機チ
タン化合物の処理蒸気と水蒸気とをこの無機質繊維に連
続的に接触させているから、上記有機チタン化合物が加
水分解−縮合重合反応を受けて無機質繊維表面に無定形
チタン化合物の保護被膜が形成され、無機質繊維の機械
的、化学的劣化を抑えて初期強度を維持した強度の大き
な無機質繊維を得ることができる。
In the present invention, as described above, inorganic fibers immediately after cotton production are fed into a surface treatment tank, and an organic titanium compound having the general formula T1(OR)4 [R2C4H9, C3H7, C2H5] is prepared. Since the inorganic fibers are continuously brought into contact with the treatment steam and water vapor, the organic titanium compound undergoes a hydrolysis-condensation polymerization reaction to form a protective film of an amorphous titanium compound on the surface of the inorganic fibers. It is possible to obtain high-strength inorganic fibers that maintain initial strength by suppressing mechanical and chemical deterioration of the fibers.

また気相処理を行なうために繊維間の微細な空間にも処
理蒸気及び水蒸気がスムーズに拡散浸透し、繊維表面に
均一な保護被膜を施し得る利点がある。
Further, since the gas phase treatment is performed, the treatment vapor and water vapor can smoothly diffuse and permeate into the fine spaces between the fibers, and there is an advantage that a uniform protective coating can be applied to the fiber surface.

しかもこの処理に際し本発明は無機質繊維の移送方向に
対する水蒸気と処理蒸気との濃度比に勾配をもたせであ
るから、皮膜自体の内層部と表層部とで特性に差をもた
せることができるものであって、この濃度比の勾配を種
々に設定することにより用途に応じた種々の特性の皮膜
を形成し得る利点がある。
Moreover, during this treatment, the present invention creates a gradient in the concentration ratio of water vapor and treatment steam in the direction of transport of the inorganic fibers, so it is possible to create a difference in properties between the inner layer and the surface layer of the film itself. Therefore, by setting the gradient of this concentration ratio variously, there is an advantage that films having various characteristics depending on the application can be formed.

例えば図示例のように水蒸気流を向流にして、無機質繊
維が表面処理槽に送り込まれた直後の時点の上記濃度比
よりも、無機質繊維が表面処理槽より搬出される直前で
の濃度比が高くなるようにしておけば、上述のように皮
膜生成初期は水蒸気濃度が低いために耐アルカリ性のよ
い皮膜となり、皮膜生成後期は水蒸気濃度が高くなって
硬度の大きな皮膜が層成され、全体として機械的強度が
大きく耐アルカリ性の良好な優れた保護皮膜が得られる
ものである。
For example, as shown in the illustrated example, when the water vapor flow is made countercurrent, the concentration ratio just before the inorganic fibers are carried out from the surface treatment tank is higher than the above concentration ratio immediately after the inorganic fibers are sent into the surface treatment tank. As mentioned above, in the early stages of film formation, the water vapor concentration is low, resulting in a film with good alkali resistance, and in the later stages of film formation, the water vapor concentration increases and a hard film is formed. An excellent protective film with high mechanical strength and good alkali resistance can be obtained.

尚、皮膜の厚さは処理時間に比例して増大するので、例
えば表面処理槽の回転数を調整して無機質繊維の移送速
度を変えることにより容易に調整することができる。
Since the thickness of the film increases in proportion to the treatment time, it can be easily adjusted by, for example, adjusting the rotation speed of the surface treatment tank and changing the transport speed of the inorganic fibers.

以下本発明を実施例に基づいて具体的に説明する。The present invention will be specifically described below based on examples.

〔実施例〕〔Example〕

Sio2:40重量%、can:40重量% A403
’15重量弧MgO: 5重量係からなるロックウー
ル組成の鉱物材料を1500℃の電気炉で溶融し、該溶
融材料を円盤法で製綿した。
Sio2: 40% by weight, can: 40% by weight A403
'15 weight arc MgO: A mineral material having a rock wool composition consisting of 5 weight arcs was melted in an electric furnace at 1500°C, and the molten material was made into cotton by the disk method.

使用した製綿用円盤は直径が200mmφ、回転数が3
00Orpm処理量が0.5t/時間の条件で製綿し、
集綿箱の底部のコンベアベルト上にルーズに堆積した繊
維を400mmφX2000mmLの処理槽中にルーズ
な状態で連続的に搬入し下記条件で処理した。
The cotton manufacturing disk used had a diameter of 200 mmφ and a rotation speed of 3.
Cotton was made under the conditions of 00Orpm throughput of 0.5t/hour,
The fibers loosely deposited on the conveyor belt at the bottom of the cotton collection box were continuously conveyed in a loose state into a 400 mmφ x 2000 mmL treatment tank and treated under the following conditions.

但しガイド外筒温度を200℃、繊維の処理槽内滞留時
間を110秒とした。
However, the temperature of the guide outer cylinder was 200° C., and the residence time of the fibers in the processing tank was 110 seconds.

く表面処理材料及び条件〉 テトラブトキシチタン(Ti(OBu)4 )蒸気濃度
2000ppm キャリアガス N2 流量 501X分 温度 200°C 水蒸気濃度 3000ppm(導入口における濃度:キ
ャリアガス N2 流量 501X分 温度 200℃ 処理したガラスウールの繊維径は10〜15μφ、繊維
表面の無定形チタン化合物の平均膜厚は180Xであっ
た。
Surface treatment materials and conditions Tetrabutoxy titanium (Ti(OBu)4) Vapor concentration 2000 ppm Carrier gas N2 flow rate 501X min. The fiber diameter of the glass wool was 10 to 15 μφ, and the average film thickness of the amorphous titanium compound on the fiber surface was 180×.

上記処理を行なったガラスウール及び未処理ガラスウー
ルの引張強度を測定した結果は次の通りであった。
The results of measuring the tensile strength of the glass wool subjected to the above treatment and the untreated glass wool were as follows.

1)未処理ガラスウール 85ky/mm11)
表面処理ガラスウール 195kg/mAまたセメン
トアルカリ(80°C)に40時間浸漬処理後の引張強
度は次の通りであった。
1) Untreated glass wool 85ky/mm11)
Surface-treated glass wool 195 kg/mA Also, the tensile strength after immersion treatment in cement alkali (80°C) for 40 hours was as follows.

1)未処理ガラスウール 32kg/mm11)
表面処理ガラスウール 177kg/mA尚、セメン
トアルカリはNaOH0,88g/l、 KOH3、4
5g/ Cca(on)2o、 48 g/ lのもの
を使用し、強度測定条件は次の通りとした。
1) Untreated glass wool 32kg/mm11)
Surface treated glass wool 177kg/mA In addition, cement alkali is NaOH0.88g/l, KOH3,4
5 g/Cca(on)2o, 48 g/l was used, and the strength measurement conditions were as follows.

ガラスウール長 20m7IL 引張速度 5mm/分 サンプル数 各40本 尚、テトラプロポキシチタン(T i (0C3H7)
4 )テトラエトキシチタン(T i(OC2N5)4
)についても上記と同様な条件において処理を行なうこ
とができる。
Glass wool length 20m7IL Tensile speed 5mm/min Number of samples 40 each In addition, tetrapropoxy titanium (Ti (0C3H7)
4) Tetraethoxytitanium (Ti(OC2N5)4)
) can also be processed under the same conditions as above.

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

第1図は本発明に用いる装置の一実施例の一部断面とし
た概略側面図、第2図は第1図の搬送入口と出口とを結
ぶ間の水蒸気及び処理蒸気の濃度勾配曲線、第3図は水
蒸気と処理蒸気の濃度比と硬度及び耐アルカリ性との関
係図であって、1は表面処理槽、5は無機質繊維、18
は水蒸気、19は処理蒸気を示す。
FIG. 1 is a partially cross-sectional schematic side view of an embodiment of the apparatus used in the present invention, and FIG. Figure 3 is a diagram showing the relationship between the concentration ratio of water vapor and treated steam, hardness, and alkali resistance, in which 1 is a surface treatment tank, 5 is an inorganic fiber, and 18
indicates water vapor, and 19 indicates treated steam.

Claims (1)

【特許請求の範囲】[Claims] 1 製綿直後の無機質繊維を表面処理槽内に送太し一般
式が’I” r (0R)4 CR” C4H9t C
3H7,C2H5]であられされる有機チタン化合物の
処理蒸気と水蒸気とをこの無機質繊維に連続的に接触さ
せると共に無機質繊維の移送方向に対する上記水蒸気と
処理蒸気との濃度比に勾配をもたせることを特徴とする
無機質繊維の強化方法。
1. Immediately after cotton production, the inorganic fiber is sent into a surface treatment tank and the general formula is 'I" r (0R) 4 CR" C4H9t C
3H7, C2H5] and water vapor are brought into continuous contact with the inorganic fibers, and a gradient is created in the concentration ratio of the water vapor and the processing vapor with respect to the direction of transport of the inorganic fibers. A method for reinforcing inorganic fibers.
JP51098041A 1976-08-14 1976-08-14 Method for reinforcing inorganic fibers Expired JPS5939382B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP51098041A JPS5939382B2 (en) 1976-08-14 1976-08-14 Method for reinforcing inorganic fibers

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP51098041A JPS5939382B2 (en) 1976-08-14 1976-08-14 Method for reinforcing inorganic fibers

Publications (2)

Publication Number Publication Date
JPS5324425A JPS5324425A (en) 1978-03-07
JPS5939382B2 true JPS5939382B2 (en) 1984-09-22

Family

ID=14209002

Family Applications (1)

Application Number Title Priority Date Filing Date
JP51098041A Expired JPS5939382B2 (en) 1976-08-14 1976-08-14 Method for reinforcing inorganic fibers

Country Status (1)

Country Link
JP (1) JPS5939382B2 (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP7340893B1 (en) * 2022-12-12 2023-09-08 有限会社マー・ファクトリー Glass wool sheet, thermoplastic resin composite material containing glass fiber, and manufacturing method thereof

Also Published As

Publication number Publication date
JPS5324425A (en) 1978-03-07

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