JPS597657B2 - Inorganic fiber surface treatment method - Google Patents
Inorganic fiber surface treatment methodInfo
- Publication number
- JPS597657B2 JPS597657B2 JP51070623A JP7062376A JPS597657B2 JP S597657 B2 JPS597657 B2 JP S597657B2 JP 51070623 A JP51070623 A JP 51070623A JP 7062376 A JP7062376 A JP 7062376A JP S597657 B2 JPS597657 B2 JP S597657B2
- Authority
- JP
- Japan
- Prior art keywords
- fibers
- vapor
- inorganic fiber
- inorganic
- film
- 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
Links
Landscapes
- 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、製面直後の無機質繊維1に一般式がTi(O
R)nCl4−n (R−C4H,、C3H7、n=1
〜3)で表わされる有機ハロゲン化チタン化合物の蒸気
2を水蒸気3と交互に吹付けて無機質繊維1表面に加水
分解縮合反応による皮膜を形成することを特徴とする無
機質繊維表面処理方法に係り、その目的とするところは
無機質繊維の製造に際し、繊維表面に均→・つ充分な膜
厚の被膜を全繊維にコーティングせしめることができ、
無機質繊維を機械的、化学的劣化から保護することによ
って初期強度の保護効果が大きい無機質繊維を得ること
ができる無機質繊維表面処理方法を提供するにある。DETAILED DESCRIPTION OF THE INVENTION The present invention provides an inorganic fiber 1 having a general formula of Ti(O
R) nCl4-n (R-C4H,, C3H7, n=1
- 3) An inorganic fiber surface treatment method characterized in that vapor 2 of an organic halogenated titanium compound represented by formula 2 is sprayed alternately with water vapor 3 to form a film on the surface of the inorganic fiber 1 by a hydrolytic condensation reaction, The purpose is to coat all fibers with a coating of sufficient thickness and uniformity on the fiber surface during the production of inorganic fibers.
An object of the present invention is to provide an inorganic fiber surface treatment method that can obtain inorganic fibers that have a large initial strength protection effect by protecting the inorganic fibers from mechanical and chemical deterioration.
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げれば非常に
大きな引張強度(200〜300kg/ma )を有す
る。In general, inorganic fibers such as glass wool and rock wool have a very high tensile strength (200 to 300 kg/ma) if no mechanical or chemical surface damage occurs 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
皮膜がデイピング法、ロール塗布法、スプレイ法等によ
って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 films called sizing agents are uniformly applied by dipping, roll coating, spraying, etc.
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、高速気流吹付け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、繊維表面に均一な皮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. unable to
Droplets were partially attached.
このためにウール状ガラス質短繊維の強さは製綿後の機
械的接触によって著しく低下している。For this reason, the strength of wool-like glassy staple fibers is significantly reduced by mechanical contact after cotton-making.
上記の如き事情に鑑みてウール状ガラス質繊維の表面に
均一な保護皮膜を形成し、初期強度を維持する目的で例
えば、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、更
には膜厚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 the above circumstances, in order to form a uniform protective film on the surface of wool-like glass fibers and maintain initial strength, for example, immediately after cotton-making, a surface treatment agent is sprayed in vapor form on the high-temperature fiber surface. Methods of causing chemical reactions such as thermal decomposition in fibers are being considered, but at present, satisfactory results have not been obtained because the film attached to the fiber surface is not uniform or thick enough. be.
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
速気流又は火災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 can be blown away by high-speed air currents or fire and become 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、更に樹脂等を吹付けてボードに加工されるか、
或いは粒子抜き、解綿、造粒等の処理を経てその他の二
次製の原料となる。These fibers are sent into a collection box by the transport air current, collected on a conveyor net, conveyor belt, etc., and transported, and then processed into a board by spraying with resin, etc.
Alternatively, it can be used as a raw material for other secondary products after undergoing processes such as particle removal, defoaming, and granulation.
以上の工程に於ける繊維強度を調べてみると、製綿直後
は200〜300kg/m4と大きく、集綿時は1 7
0 〜2 3 0kg/maとなり、更に脱粒、解綿
後は40〜100kg/m7?Lと著しく小さくなるこ
とが判明した。When examining the fiber strength in the above process, it was as high as 200 to 300 kg/m4 immediately after cotton production, and 1.7 kg/m4 during cotton collection.
0 to 230 kg/m7, and then 40 to 100 kg/m7 after shedding and opening. It was found that the value becomes significantly smaller than L.
これらの強度劣化はほとんどが繊維間の機械的接触によ
って生じ、従って繊維表面に保護皮膜を形成させること
によってこれらの強度劣化を防ぐことができる。Most of these strength deteriorations occur due to mechanical contact between fibers, and therefore, these strength deteriorations can be prevented by forming a protective film on the fiber surface.
本発明は集綿時、すなわちコンベアネット(又はコンベ
アベルト)上にゆるく(ルーズに)堆積された無機質繊
維をそのままの状態で表面処理チャンバ内に連続的に送
り込む。In the present invention, during cotton collection, inorganic fibers loosely deposited on a conveyor net (or conveyor belt) are continuously fed as they are into a surface treatment chamber.
チャンバ内に送り込まれた無機質繊維にまず有機・・ロ
ゲン化チタン( T i( OR ) nC 14
n , R−C4 H9、C3H7、n=1〜3)化合
物の蒸気をノズル等から吹付け、繊維の全表面に、繊維
帯の厚み方向に対しても均一に蒸気を吸着、付着させる
。The inorganic fibers fed into the chamber are first coated with organic titanium rogenide (Ti(OR) nC 14
n, R-C4 H9, C3H7, n=1-3) The vapor of the compound is sprayed from a nozzle or the like, and the vapor is adsorbed and adhered to the entire surface of the fibers, even in the thickness direction of the fiber strip.
これらの無機質繊維はゆっくりと連続的に移動して、次
に水蒸気を含む空気(Wet Air)、窒素等がノ
ズル等から吹付けられる。These inorganic fibers move slowly and continuously, and then wet air containing water vapor, nitrogen, etc. are blown from a nozzle or the like.
この時無機質繊維表面で例えばTi (OBu )2C
l2は加水分解縮合して容易に無定形チタン化合物皮膜
を形成するものである。At this time, for example, Ti(OBu)2C on the surface of the inorganic fiber.
12 easily forms an amorphous titanium compound film through hydrolytic condensation.
以下本発明を添付図に基づいて詳細に説明する。The present invention will be explained in detail below based on the accompanying drawings.
第1図に於いて鉱物質材料の溶融物は電気炉又はキュポ
ラ等の溶融炉から直接或いは樋を経て高速回転する分配
回転円盤上に落下させるもので、分配回転円盤によって
細分化(微粒化)され加速された溶融物は製綿円盤4に
供給される。In Figure 1, the molten mineral material is dropped from a melting furnace such as an electric furnace or a cupola directly or through a gutter onto a rotating distribution disk that rotates at high speed, and is finely divided (atomized) by the rotating distribution disk. The accelerated melt is supplied to the cotton making disk 4.
製綿円盤4上で繊維生成粒子ができ、遠心力によって無
機質繊維1が円周方向に形成される。Fiber-forming particles are formed on the cotton-making disk 4, and inorganic fibers 1 are formed in the circumferential direction by centrifugal force.
これらの無機質繊維1は製綿円盤4の後方に取付けられ
ているエアーリング(搬送用気体噴出リング)5によっ
て90度方向転換して集綿箱6に集められる。These inorganic fibers 1 are turned 90 degrees by an air ring (carrying gas jet ring) 5 attached to the rear of the cotton making disk 4 and collected in a cotton collection box 6.
また粒子(ショット)7はエアーによって方向転換され
ることなく円周方向に飛散するため、無機質繊維1から
分離される。Furthermore, since the particles (shots) 7 are scattered in the circumferential direction without being changed in direction by air, they are separated from the inorganic fibers 1.
集綿箱6の底部は矢印で示す向きに動くようにローラ部
片8で支えられた網目のコンベアベルト9かラ成ってい
る。The bottom of the cotton collection box 6 consists of a mesh conveyor belt 9 supported by roller pieces 8 so as to move in the direction indicated by the arrow.
コンベアベルト9上に堆積した無機質繊維1は表面処理
チャンバ10内に輸送される。The inorganic fibers 1 deposited on the conveyor belt 9 are transported into a surface treatment chamber 10.
表面処理チャンバ10は数個の処理蒸気箱11と水蒸気
箱12を交互に連結してできていて、各々の箱の上部に
は有機ハロゲン化チタン化合物の蒸気2、水蒸気3を噴
出するノズル13,14が取付けられている。The surface treatment chamber 10 is made up of several processing steam boxes 11 and steam boxes 12 connected alternately, and at the top of each box there are nozzles 13 for spouting organic halogenated titanium compound vapor 2 and water vapor 3. 14 is installed.
表面処理チャンバ10の底部のコンベアベルト90部分
には吸引箱15をその開いた側が上部ベルトの下面に隣
接するように設置され任意の適当な空気排出装置に連結
されてある。At the bottom of the surface treatment chamber 10, a section of the conveyor belt 90 has a suction box 15 installed with its open side adjacent the underside of the upper belt and connected to any suitable air evacuation device.
また第2図に於いて製綿後、コンベアベルト9上に堆積
された強度劣化の著し《小さい無機質繊維1はコンベア
ベルト9によって処理蒸気箱11に搬送され、そこで有
機ハロゲン化チタン化合物の蒸気2がノズル13から噴
射される。In addition, in FIG. 2, after cotton-making, the small inorganic fibers 1 deposited on the conveyor belt 9 with significant strength deterioration are transported by the conveyor belt 9 to the processing steam box 11, where the organic halogenated titanium compound 2 is injected from the nozzle 13.
繊維表面に充分処理材蒸気を吸着した無機質繊維1は次
に水蒸気箱12に搬送され、ここでも同様なノズル14
から水蒸気3を含んだ気体が噴射される。The inorganic fiber 1 that has sufficiently adsorbed the processing material vapor on the fiber surface is then conveyed to the steam box 12, where it is also passed through the same nozzle 14.
A gas containing water vapor 3 is injected from the tank.
これによって繊維表面では有機ハロゲン化チタン化合物
は容易に加水分解縮合して無定形チタン化合物膜を生成
する。As a result, the organic halogenated titanium compound is easily hydrolyzed and condensed on the fiber surface to form an amorphous titanium compound film.
更にこれらの繊維は次の処理蒸気箱11に搬送され前記
と同様な処理を受け、更に水蒸気箱12に搬送されて加
水分解縮合し、これらの処理を繰返すことによって繊維
表面の膜厚は次第に増大していく。Furthermore, these fibers are transported to the next processing steam box 11 and subjected to the same treatment as described above, and further transported to the steam box 12 where they are hydrolyzed and condensed, and by repeating these treatments, the film thickness on the fiber surface gradually increases. I will do it.
有機ハロゲン化チタン化合物はT I ( ocs H
7)nc i 4nの方がTi(OC4H,)nC14
−n よりも加水分解しやすく処理条件における有機・
・ロゲン化チタン化合物の蒸気2に対する最適水蒸気濃
度は異なるが、たとえば有機ハロゲン化チタン化合物の
蒸気2を蒸気濃度2 0 0 0 ppm蒸気温度20
0℃で乾燥空気などをキャリャガスとして流量50l/
分でノズル13から噴射させる場合には、水蒸気3は濃
度10000ppm,温度200℃で空気または窒素な
どをキャリャガスとして流量50l/分でノズル14か
ら噴射させることによりすべての有機ハロゲン化チタン
化合物に対して水蒸気が過剰となり充分に加水分解縮合
させることができる。Organic titanium halide compounds are T I ( ocs H
7) nc i 4n is more Ti(OC4H,)nC14
-N is more easily hydrolyzed than organic
・The optimum water vapor concentration for the vapor 2 of the titanium halogenide compound is different, but for example, the optimum water vapor concentration for the vapor 2 of the organic titanium halide compound is 2000 ppm and the vapor temperature is 20.
Flow rate 50l/dry air etc. as carrier gas at 0℃
When injecting the water vapor 3 from the nozzle 13 at a concentration of 10,000 ppm and a temperature of 200° C., the water vapor 3 is injected from the nozzle 14 at a flow rate of 50 l/min using air or nitrogen as a carrier gas to completely eliminate all organic halogenated titanium compounds. Water vapor is in excess and sufficient hydrolysis and condensation can be carried out.
尚ノズル13,14から噴出された気体は第2図のよう
に円錐状の噴流になっていて、繊維との交差点が円にな
り、これらの円は隣同志が接するようになっている。The gases ejected from the nozzles 13 and 14 form conical jets as shown in FIG. 2, and the intersections with the fibers form circles, with adjacent circles touching each other.
これによって繊維の流れ方向は勿論、厚さの方向に対し
ても均一に蒸気に吸着させることができる。This allows the fibers to be uniformly adsorbed by steam not only in the flow direction of the fibers but also in the thickness direction.
また処理剤が液体の粒子でなく、気体であることによっ
ても上記の均一性が更に高められる。Furthermore, the above-mentioned uniformity can be further improved by using the processing agent as a gas instead of liquid particles.
本発明にあっては上述のように製綿直後の無機質繊維に
一般式がTi (OR)ncl4 , (R=C4
H,、C3H7、n = 1 〜3 )であらわされる
有機・・ロゲン化チタン化合物の蒸気を水蒸気と交互に
吹付けて無機質繊維表面に加水分解縮合反応による皮膜
を形成しているから、スプレー法による液滴の散布と異
なり、気相処理であるため繊維間の狭い空隙にも充分蒸
気が浸透し、長繊維の場合は勿論のこと、短繊維の場合
でも全繊維表面にチタン化合物の皮膜を形成することが
できるものであって、製綿直後の大きな初期強度の劣化
を防止し、強度の大きな無機質繊維が得ることができろ
ものである。In the present invention, as mentioned above, the general formula of the inorganic fiber immediately after cotton production is Ti(OR)ncl4, (R=C4
Since the vapor of an organic titanium halogenide compound represented by H, C3H7, n = 1 to 3) is sprayed alternately with water vapor to form a film by a hydrolytic condensation reaction on the surface of the inorganic fiber, it is a spray method. Unlike the spraying of droplets, the vapor phase treatment allows the steam to penetrate into the narrow spaces between the fibers, creating a titanium compound coating on the surface of all fibers, not only long fibers but also short fibers. It is possible to form inorganic fibers with high strength by preventing a large deterioration of the initial strength immediately after cotton making.
また同じ気相処理法で気相熱分解法があるが、処理時間
が製造直後の無機質繊維の冷却時間によって短期間に制
限されるが、本発明にあっては高温を必要としないため
処理時間を充分に長くとれ充分に厚い補強保護効果の充
分な皮膜を生成させることができる。In addition, there is a vapor-phase pyrolysis method, which is the same vapor-phase processing method, but the processing time is limited to a short period due to the cooling time of the inorganic fibers immediately after production, but the present invention does not require high temperatures, so the processing time is It is possible to produce a sufficiently long and sufficiently thick film with sufficient reinforcing and protective effect.
しかも有機ノ・ロゲン化チタン化合物と水蒸気とを交互
に吹付けるようにしているから、無機質繊維の処理時の
損傷の程度或いは使用目的等に応じて、交互に行なう吹
付ける処理回数の増減により簡単に処理皮膜の厚さを最
適なものに調節することができる。Moreover, since the organic titanium compound and water vapor are sprayed alternately, the number of alternating spraying treatments can be easily increased or decreased depending on the degree of damage during treatment of inorganic fibers or the purpose of use. The thickness of the treated film can be adjusted to the optimum thickness.
尚、本発明に於いて有機ハロゲン化チタン化合物の蒸気
と水蒸気を同時噴射させると無機質繊維表面に蒸気が到
達する以前に加水分解が起こり、それによって生じた白
粉が無機質繊維表面にゆるく付着するが、容易に脱着し
保護膜とならない。In addition, in the present invention, when vapor of an organic halogenated titanium compound and water vapor are simultaneously injected, hydrolysis occurs before the vapor reaches the surface of the inorganic fiber, and the resulting white powder loosely adheres to the surface of the inorganic fiber. , it is easily attached and detached and does not form a protective film.
また有機・・ロゲン化チタン化合物の蒸気と水蒸気を別
々に各各長時間処理しても皮膜の厚さは変わりなく、し
かも膜厚は不充分であり、こにも保護効果は少ない。Moreover, even if the vapor of the organic titanium chloride compound and the water vapor are treated separately for a long time, the thickness of the film remains the same, and the film thickness is insufficient, so that the protective effect is also small.
したがって有機・・ロゲン化チタン化合物の蒸気と水蒸
気を交互に数回処理することによって機械的、化学的損
傷に耐えうるに充分な膜厚を得ることができる。Therefore, a film thickness sufficient to withstand mechanical and chemical damage can be obtained by alternately treating the film with vapor of an organic titanium chloride compound and water vapor several times.
この方法で得られた繊維上の皮膜は熱可塑性樹脂の皮膜
のような硬さをもち、繊維同志を接着させることもない
。The film on the fibers obtained by this method has a hardness similar to that of a thermoplastic resin film, and does not cause fibers to adhere to each other.
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
Si0240重量%、Ca040重量%、AI2031
5重量%、Mg0 5重量%からなるガラス組成のガラ
スウール材料を1500℃の電気炉で溶融し、該溶融材
料を製綿用円盤径が200φ、回転数が3000rpm
、処理量が0.5t/時間の条件で製綿し、集綿箱の底
部のコンベアネット上にルーズに堆積した繊維に下記処
理材料の蒸気と水蒸気を別々のノズルから順次交互に各
々5回ずつ吹付けた。Example Si0240% by weight, Ca040% by weight, AI2031
A glass wool material having a glass composition consisting of 5% by weight and 5% by weight of Mg0 was melted in an electric furnace at 1500°C, and the molten material was heated to a cotton manufacturing disk with a diameter of 200φ and a rotation speed of 3000 rpm.
, Cotton was produced under the condition that the processing amount was 0.5 t/hour, and the steam and water vapor of the following treatment materials were sequentially and alternately applied to the fibers loosely deposited on the conveyor net at the bottom of the cotton collection box from separate nozzles, 5 times each. I sprayed it one by one.
く処理材料〉
以上のように処理されたガラスウールの繊維径は10〜
15μφであった。Treated material〉 The fiber diameter of the glass wool treated as above is 10~
It was 15μφ.
繊維表面膜厚は約5 ooAであった。The fiber surface film thickness was about 5 ooA.
これらのガラスウーノレの引弘り強度を測定した結果、 であった。As a result of measuring the expansion strength of these glass wolves, Met.
ここで引張強度測定条件は次の通りとした。The tensile strength measurement conditions were as follows.
第1図は本発明の一実施例の概略工程説明図、第2図は
同上の一部省略斜視図であって、1は無機質繊維、2は
有機・・ロゲン化チタン化合物、3は水蒸気を示す。FIG. 1 is a schematic process explanatory diagram of an embodiment of the present invention, and FIG. 2 is a partially omitted perspective view of the same, in which 1 is an inorganic fiber, 2 is an organic titanium rogenide compound, and 3 is a water vapor show.
Claims (1)
OR ) nC 14−n( R =C4H9、C3H
7、n=1〜3)で表わされる有機ハロゲン化チタン化
合物の蒸気を水蒸気と交互に吹付けて無機質繊維表面に
加水分解縮合反応による皮膜を形成することを特徴とす
る無機質繊維表面処理方法。1 The general formula T i (
OR ) nC 14-n ( R = C4H9, C3H
7. An inorganic fiber surface treatment method, which comprises spraying vapor of an organic halogenated titanium compound represented by n=1 to 3) alternately with water vapor to form a film on the surface of the inorganic fiber by a hydrolytic condensation reaction.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP51070623A JPS597657B2 (en) | 1976-06-15 | 1976-06-15 | Inorganic fiber surface treatment method |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP51070623A JPS597657B2 (en) | 1976-06-15 | 1976-06-15 | Inorganic fiber surface treatment method |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS52155297A JPS52155297A (en) | 1977-12-23 |
| JPS597657B2 true JPS597657B2 (en) | 1984-02-20 |
Family
ID=13436919
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP51070623A Expired JPS597657B2 (en) | 1976-06-15 | 1976-06-15 | Inorganic fiber surface treatment method |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS597657B2 (en) |
-
1976
- 1976-06-15 JP JP51070623A patent/JPS597657B2/en not_active Expired
Also Published As
| Publication number | Publication date |
|---|---|
| JPS52155297A (en) | 1977-12-23 |
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