JPH0428767B2 - - Google Patents
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- Publication number
- JPH0428767B2 JPH0428767B2 JP18318287A JP18318287A JPH0428767B2 JP H0428767 B2 JPH0428767 B2 JP H0428767B2 JP 18318287 A JP18318287 A JP 18318287A JP 18318287 A JP18318287 A JP 18318287A JP H0428767 B2 JPH0428767 B2 JP H0428767B2
- Authority
- JP
- Japan
- Prior art keywords
- mold
- molding material
- tank
- flow
- molding
- 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
- 239000000835 fiber Substances 0.000 claims description 56
- 239000012778 molding material Substances 0.000 claims description 36
- 238000000465 moulding Methods 0.000 claims description 23
- 238000000034 method Methods 0.000 claims description 21
- 238000003756 stirring Methods 0.000 claims description 17
- 230000002093 peripheral effect Effects 0.000 claims description 15
- 230000003014 reinforcing effect Effects 0.000 claims description 8
- 239000007864 aqueous solution Substances 0.000 claims description 7
- 239000012783 reinforcing fiber Substances 0.000 claims description 4
- 239000004744 fabric Substances 0.000 description 11
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 description 8
- 229920000049 Carbon (fiber) Polymers 0.000 description 6
- 239000004917 carbon fiber Substances 0.000 description 6
- 238000004519 manufacturing process Methods 0.000 description 6
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 6
- 238000001035 drying Methods 0.000 description 4
- 238000010304 firing Methods 0.000 description 4
- 238000007796 conventional method Methods 0.000 description 3
- 230000000694 effects Effects 0.000 description 3
- 229910000838 Al alloy Inorganic materials 0.000 description 2
- XKRFYHLGVUSROY-UHFFFAOYSA-N Argon Chemical compound [Ar] XKRFYHLGVUSROY-UHFFFAOYSA-N 0.000 description 2
- 239000012300 argon atmosphere Substances 0.000 description 2
- 239000012298 atmosphere Substances 0.000 description 2
- 239000011230 binding agent Substances 0.000 description 2
- 239000011159 matrix material Substances 0.000 description 2
- 238000003825 pressing Methods 0.000 description 2
- 239000004576 sand Substances 0.000 description 2
- RMAQACBXLXPBSY-UHFFFAOYSA-N silicic acid Chemical compound O[Si](O)(O)O RMAQACBXLXPBSY-UHFFFAOYSA-N 0.000 description 2
- 239000011800 void material Substances 0.000 description 2
- 230000037303 wrinkles Effects 0.000 description 2
- 239000004677 Nylon Substances 0.000 description 1
- 238000004026 adhesive bonding Methods 0.000 description 1
- 239000002518 antifoaming agent Substances 0.000 description 1
- 229910052786 argon Inorganic materials 0.000 description 1
- 230000003139 buffering effect Effects 0.000 description 1
- 238000001354 calcination Methods 0.000 description 1
- 238000005266 casting Methods 0.000 description 1
- 239000000470 constituent Substances 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000009826 distribution Methods 0.000 description 1
- 239000003733 fiber-reinforced composite Substances 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 239000011261 inert gas Substances 0.000 description 1
- 230000001050 lubricating effect Effects 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 229920001778 nylon Polymers 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 230000035699 permeability Effects 0.000 description 1
- 238000002360 preparation method Methods 0.000 description 1
- 238000007788 roughening Methods 0.000 description 1
- 239000004094 surface-active agent Substances 0.000 description 1
- 239000010409 thin film Substances 0.000 description 1
- 230000004580 weight loss Effects 0.000 description 1
Landscapes
- Manufacture Of Alloys Or Alloy Compounds (AREA)
- Paper (AREA)
- Producing Shaped Articles From Materials (AREA)
- Manufacturing Of Tubular Articles Or Embedded Moulded Articles (AREA)
Description
A 発明の目的
(1) 産業上の利用分野
本発明は強化用筒状繊維成形体の成形方法、特
に、強化用繊維を含む成形材料の水溶液を収容す
るタンク内に立設された通気性筒状成形型内に吸
引作用を施し、成形材料を成形型の外周面に付着
させて前記繊維成形体を成形する方法の改良に関
する。
(2) 従来の技術
従来、この種成形方法として、タンク内に配設
された撹拌羽根を回転させて成形材料を撹拌する
といつた手法が知られている(特開昭61−126357
号公報参照)。
(3) 発明が解決しようとする問題点
前記従来方において、成形材料の撹拌を十分に
行うためには、撹拌羽根の回転速度を早めて渦状
の成形材料の流れを形成すればよいが、このよう
にすると成形型の外周に沿つて成形材料が急速に
流れるため、成形型に対する成形材料の付着性が
悪く、また付着した成形材料が前記流れによつて
取去られるといつた問題があり、したがつて繊維
成形体の生産能率が悪く、また均一な厚さを有す
る繊維成形体を得ることが難しい。
本発明は前記に鑑み、繊維成形体の生産能率を
向上させ、また厚さの均一な繊維成形体を得るこ
とのできる前記成形方法を提供することを目的と
する。
B 発明の構成
(1) 問題点を解決するための手段
本発明は、強化用繊維を含む成形材料の水溶液
を収容するタンク内に立設された通気性筒状成形
型内に吸引作用を施し、前記成形材料を該成形型
の外周面に付着させて強化用筒状繊維成形体を成
形するに当り、不動に保持された前記成形型の軸
線回りにおける前記タンクの回転および該タンク
内周面またはその近傍に存する複数の撹拌羽根の
撹拌作用によりタンク内周面近傍にその周方向に
沿う乱流状態の成形材料の流れを形成し、前記成
形型の外周に配設される複数の整流板に前記成形
材料の流れを衝突させて、該流れを前記成形型の
外周面に向う層流に変換することを特徴とする。
(2) 作用
前記のようにタンク内周面近傍において、乱流
状態の成形材料の流れを形成すると、タンク内底
部における成形材料の澱みを防止することができ
る。
乱流状態の成形材料の流れが各整流板に衝突す
ると、その流れは流速を弱められ、また成形型内
に吸引作用が施されていることもあつて、成形型
の外周面に向かう層流に変換される。これにより
成形型に対する成形材料の付着性が良好となり、
また付着した成形材料が、その流れによつて取去
られることも殆どない。
(3) 実施例
第1図は成形工程、乾燥工程、焼成工程等を経
て得られた強化用筒状繊維成形体1を示し、その
繊維成形体1は、強化用繊維としての、炭素繊維
およびアルミナ繊維の混合短繊維を、無機バイン
ダとしてのシリカゾル、アルミナゾル、またはそ
れらの混合ゾルにより部分的に結合したもので、
マトリツクスが浸入し得る無数の空〓を有する。
この繊維成形体1は、例えばアルミニウム合金
製シリンダブロツクの鋳造時においてアルミニウ
ム合金マトリツクスと複合して繊維強化複合シリ
ンダスリーブを得るために用いられる。この場
合、炭素繊維は主としてその潤滑能によりシリン
ダスリーブ内周面の摺動特性向上に、またアルミ
ナ繊維は主としてシリンダボア回りの強度向上に
それぞれ寄与する。
前記繊維成形体1は第2図に示す製造工程を経
て得られる。
第2図aにおいて、成形型2はシエル砂(粒度
AFS35)を用いて通気性を有する円筒状に形成
されたもので、330〜480℃に加熱されると完全に
崩壊するという物性を有する。
先ず、成形型2の外周面前体を、通気性を有
し、且つ成形型2の崩壊温度で焼失する薄膜体、
例えば、6−ナイロンよりなる厚さ0.10mmでメリ
ヤス編みの伸縮性薄布Fにより覆う。
第2図bに示すように、成形型2の両端開口部
にそれぞれホルダ31、32を接着、ボルト締め等に
より取付けてそれら開口部を密封する。
第2図cに示すように、炭素繊維およびアルミ
ナ繊維の混合短繊維、アルミナゾル等を含む成形
材料の水溶液を収容した、成形装置4の円筒状タ
ンク5内に成形型2を立設し、揚水ポンプ6によ
り成形型2内にホルダ32の開口部7を通じて吸引
作用を施し、成形材料を薄布Fを介して成形型2
の外周面に所定の厚さに付着させ、繊維成形体1
を成形する。この揚水ポンプ6による成形作業は
略2分間に亘つて行われる。
第2図dに示すように、成形型2をラバープレ
スの耐圧容器8内に設置し、空圧源9より加圧空
気を耐圧容器8内に供給してラバー10を介し繊
維成形体1を成形型2の外周面に10Kg/cm2の圧力
を以て押圧し、これにより繊維成形体1の形状を
整え、同時に繊維体積率を決定する。
この場合、成形型2が前記押圧力により僅かに
縮径するが、その縮径動作には薄布Fがその収縮
作用により追随するので、薄布Fに皺が発生する
ことがなく、したがつて皺の転写による繊維成形
体1内周面の粗面化を防止することができる。前
記押圧力が解除された後は、成形型2が元の状態
に復元するが、このときは薄布Fが伸張するので
何等支障を来たすことはない。
第2図eに示すように、成形型2より両ホルダ
31,32を取外す。
第2図fに示すように、成形型2を空気雰囲気
に保たれた乾燥炉11内に設置し、繊維成形体1
に炉内温度120℃にて60分間の乾燥処理を施し
て水分を蒸発除去する。この加熱乾燥処理中に薄
布Fが焼失を開始する。また成形型2が膨脹する
が、その膨脹量は薄布Fの一部焼失により生じた
空〓および残りの薄布Fの緩衝作用によつて吸収
されるので、繊維成形体1に、成形型2の膨脹に
起因したクラツクが発生することがない。
第2図gに示すように、成形型2を、空気雰囲
気に保たれた焼成炉12内に設置し、成形型2に
炉内温度450℃にて30分間の崩壊処理を施し、そ
の昇温過程で薄布Fを完全に焼失させる。この崩
壊処理により成形型2は100%崩壊する。
前記成形型2は、その崩壊に先立つて膨張する
が、その膨張量は薄布Fの焼失に伴つて生じた空
〓gにより吸収され、したがつて前記同様に繊維
成形体1にクラツクが発生することがない。
また繊維成形体1は薄布Fを介して成形型2に
接しているので、成形型2の崩壊後その構成材料
であるシエル砂が繊維成形体1に付着して残留す
ることがなく、したがつて繊維成形体1内周面が
平滑となる。
第2図hに示すように、今度は繊維成形体1の
みをアルゴン雰囲気に保たれた焼成炉12内に設
置し、その繊維成形体1に炉内温度800℃にて30
分間の焼成処理を施して、アルミナゾルにより混
合短繊維を部分的に結合する。この場合、焼成処
理をアルゴン雰囲気中で行うので、炭素繊維の酸
化が回避され、その減量が防止される。なお、ア
ルゴンに代えて他の不活性ガスを用いてもよい。
次に、第3、第4図により本発明成形方法の実
施に用いられる成形装置4について詳述する。
成形材料の水溶液Lを収容するタンク5は、上
面を開口されると共に底部外面に中空軸部13を
有し、その中空軸部13は軸受14を介して基台
15に形成された孔部16に支持される。成形型
2をタンク5内に立設すべく、上端に取付フラン
ジ17を備えた中空棒体18が中空軸部13に、
シール部材19を介して挿通される。
中空軸部13は図示しない駆動源に連結され、
また中空棒体18は基台15に固定されると共に
その通孔20は揚水ポンプ6に接続される。成形
型2は、その一方のホルダ32の開口部7を通孔2
0に合致させて中空棒体18の取付フランジ17
上に着脱自在に立設され、したがつて成形型2は
タンク5内に不動に保持されると共にタンク5は
成形型2の軸線回りに回転可能に構成される。
成形型2の外周において、その成形型2の軸線
方向および放射方向に延びる複数の整流板21が
円周方向に等間隔で配設される。各整流板21の
上端は環状取付板22を介してタンク5を覆うカ
バー23の環状天井面に固着され、また各下端は
タンク5の底部近傍に配置される。カバー23は
基台15上面に複数のボルト24により固定され
ており、したがつて各整流板21は成形型2の外
周に不動に配設される。
各整流板21の、成形型2半径方向外側面を通
る仮想円C(第4図)とタンク5内周面との間に、
軸線方向に複数の撹拌羽根251を備えた複数の
回転軸26がタンク5の周方向に沿つて配設さ
れ、各回転軸26を駆動するモータ27がカバー
23の頂面に固定される。
繊維成形体1の成形作業に当つては、例えばタ
ンク5および各撹拌羽根251を第4図時計方向
に回転させ、また揚水ポンプ6を作動して成形型
2内に吸引作用を施す。
これによりタンク5内周面近傍では、タンク5
の回転と各撹拌羽根251による撹拌作用によつ
て成形材料の流れが乱流状態となり、成形材料が
タンク5内底部に澱むことがない。
乱流状態の成形材料の流れが各整流板21に衝
突すると、その流れは流速を弱められ、また成形
型2内に吸引作用が施されていることもあつて、
第4図矢印で示すように成形型2の外周面に向か
う層流に変換される。これにより成形型2に対す
る成形材料の付着性が良好となり、また付着した
成形材料が、その流れによつて取去られることも
殆どない。したがつて繊維成形体1の生産能率を
向上させ、また厚さの均一な繊維成形体1が得ら
れる。
次に繊維成形体1の実施例について説明する。
(a) 成形材料の水溶液Lの調製
強化用繊維として平均直径18μm、平均長さ
0.8mmの炭素繊維0.02〜0.20重量%および平均直
径3〜4μm、平均長さ100〜200μmのアルミナ
繊維0.22〜0.40重量%と、無機バインダとして
のシリカゾルまたはアルミナゾル4〜6重量%
と、消泡剤および界面活性剤を合せて0.2重量
%と、水93.4〜95.4重量%(32)とを混合す
る。このようにして得られた成形材料のタンク
5内における、計算上の繊維濃度は4.2g/Kg
である。
(b) 成形型2の寸法
上部外径78mm、下部外径74mm、厚さ5mmであ
る。
前記成形材料の水溶液Lおよび成形型2を用
い、表の条件の下に前記装置4により二種類の
繊維成形体1を成形する。
A. Purpose of the invention (1) Industrial field of application The present invention relates to a method for molding a reinforcing cylindrical fiber molded article, and in particular, to a method for molding a reinforcing cylindrical fiber molded article, and in particular, to a method for molding a reinforcing cylindrical fiber molded article, and in particular, to a method for molding a reinforcing cylindrical fiber molded article. The present invention relates to an improvement in a method for molding the fiber molded article by applying a suction action inside a shaped mold and causing a molding material to adhere to the outer peripheral surface of the mold. (2) Prior art Conventionally, as a molding method of this type, a method is known in which the molding material is stirred by rotating a stirring blade disposed in a tank (Japanese Patent Application Laid-Open No. 126357-1982).
(see publication). (3) Problems to be solved by the invention In the conventional method described above, in order to sufficiently stir the molding material, it is sufficient to increase the rotational speed of the stirring blade to form a spiral flow of the molding material. In this case, the molding material flows rapidly along the outer periphery of the molding die, resulting in poor adhesion of the molding material to the molding die, and the adhering molding material may be removed by the flow. Therefore, the production efficiency of fiber molded bodies is poor, and it is difficult to obtain fiber molded bodies having a uniform thickness. In view of the above, an object of the present invention is to provide the above-mentioned molding method which can improve the production efficiency of fiber molded bodies and obtain fiber molded bodies having a uniform thickness. B. Structure of the Invention (1) Means for Solving Problems The present invention provides a method for applying a suction action to an air-permeable cylindrical mold that is installed upright in a tank containing an aqueous solution of a molding material containing reinforcing fibers. , when attaching the molding material to the outer peripheral surface of the mold and molding the reinforcing cylindrical fiber molded article, rotation of the tank around the axis of the mold held immovably and the inner peripheral surface of the tank; or a plurality of rectifying plates disposed around the outer periphery of the mold, forming a turbulent flow of the molding material along the circumferential direction near the inner peripheral surface of the tank due to the stirring action of a plurality of stirring blades existing in the vicinity; The method is characterized in that the flow of the molding material collides with the flow of the molding material to convert the flow into a laminar flow toward the outer peripheral surface of the mold. (2) Effect By forming a turbulent flow of the molding material near the inner peripheral surface of the tank as described above, stagnation of the molding material at the inner bottom of the tank can be prevented. When the turbulent flow of molding material collides with each straightening plate, the flow velocity is weakened, and also because there is a suction effect inside the mold, the flow becomes laminar toward the outer circumferential surface of the mold. is converted to This improves the adhesion of the molding material to the mold,
Furthermore, the adhered molding material is hardly removed by the flow. (3) Example Figure 1 shows a reinforcing cylindrical fiber molded body 1 obtained through a molding process, a drying process, a firing process, etc. The fiber molded body 1 contains carbon fibers and carbon fibers as reinforcing fibers. Mixed short fibers of alumina fibers are partially bonded by silica sol, alumina sol, or a mixed sol thereof as an inorganic binder.
There are countless spaces into which the matrix can penetrate. This fiber molded body 1 is used, for example, in order to obtain a fiber-reinforced composite cylinder sleeve by combining it with an aluminum alloy matrix when casting an aluminum alloy cylinder block. In this case, the carbon fibers mainly contribute to improving the sliding characteristics of the inner circumferential surface of the cylinder sleeve due to their lubricating ability, and the alumina fibers mainly contribute to improving the strength around the cylinder bore. The fiber molded body 1 is obtained through the manufacturing process shown in FIG. In Figure 2a, the mold 2 is made of shell sand (grain size
It is formed into a breathable cylindrical shape using AFS35), and has the property of completely collapsing when heated to 330-480°C. First, the outer peripheral surface of the mold 2 is made of a thin film body that has air permeability and burns out at the collapse temperature of the mold 2;
For example, it is covered with a stockinette-knit stretchable thin fabric F made of 6-nylon and having a thickness of 0.10 mm. As shown in FIG. 2b, holders 3 1 and 3 2 are attached to the openings at both ends of the mold 2 by gluing, bolting, etc., and the openings are sealed. As shown in FIG. 2c, the mold 2 is set upright in a cylindrical tank 5 of the molding device 4 containing an aqueous solution of a molding material containing mixed short fibers of carbon fibers and alumina fibers, alumina sol, etc. The pump 6 applies suction into the mold 2 through the opening 7 of the holder 32 , and the molding material is transferred to the mold 2 through the thin cloth F.
to a predetermined thickness on the outer peripheral surface of the fiber molded body 1.
to form. This molding operation using the water pump 6 is performed for approximately 2 minutes. As shown in FIG. 2d, the mold 2 is placed in a pressure container 8 of a rubber press, and pressurized air is supplied from an air pressure source 9 into the pressure container 8 to mold the fiber molded product 1 through the rubber 10. The outer peripheral surface of the mold 2 is pressed with a pressure of 10 kg/cm 2 to adjust the shape of the fiber molded body 1 and at the same time determine the fiber volume fraction. In this case, the diameter of the mold 2 is slightly reduced by the pressing force, but since the thin fabric F follows the shrinking action due to its shrinking action, wrinkles do not occur in the thin fabric F. Roughening of the inner circumferential surface of the fiber molded body 1 due to transfer of wrinkles can be prevented. After the pressing force is released, the mold 2 is restored to its original state, but since the thin fabric F is stretched at this time, no problem occurs. As shown in Figure 2e, both holders are removed from the mold 2.
Remove 3 1 and 3 2 . As shown in FIG. 2f, the mold 2 is placed in a drying oven 11 kept in an air atmosphere,
A drying process is performed for 60 minutes at an oven temperature of 120°C to evaporate and remove moisture. During this heat drying process, the thin fabric F starts to burn out. Furthermore, the mold 2 expands, but the amount of expansion is absorbed by the void created by partially burning off the thin fabric F and the buffering effect of the remaining thin fabric F. No cracks will occur due to the expansion of item 2. As shown in Figure 2g, the mold 2 is placed in a firing furnace 12 maintained in an air atmosphere, and the mold 2 is subjected to a collapse treatment for 30 minutes at a furnace temperature of 450°C, and the temperature is increased. Thin cloth F is completely burned out in the process. The mold 2 collapses 100% by this collapse process. The mold 2 expands before collapsing, but the amount of expansion is absorbed by the void g generated as the thin fabric F is burned out, and as a result, cracks occur in the fiber molded product 1 in the same manner as described above. There's nothing to do. In addition, since the fiber molded body 1 is in contact with the mold 2 through the thin cloth F, the shell sand that is the constituent material of the mold 2 does not adhere to and remain on the fiber molded body 1 after the mold 2 collapses. As a result, the inner circumferential surface of the fiber molded body 1 becomes smooth. As shown in FIG. 2h, only the fiber molded body 1 is placed in a firing furnace 12 kept in an argon atmosphere, and the fiber molded body 1 is heated for 30 minutes at a furnace temperature of 800°C.
The mixed short fibers are partially bonded by the alumina sol by a calcination treatment for 1 minute. In this case, since the firing process is performed in an argon atmosphere, oxidation of the carbon fibers is avoided and their weight loss is prevented. Note that other inert gases may be used instead of argon. Next, the molding apparatus 4 used to carry out the molding method of the present invention will be described in detail with reference to FIGS. 3 and 4. The tank 5 containing the aqueous solution L of the molding material is open at the top and has a hollow shaft 13 on the outer surface of the bottom, and the hollow shaft 13 is connected to a hole 16 formed in the base 15 via a bearing 14. Supported by In order to erect the mold 2 in the tank 5, a hollow rod 18 with a mounting flange 17 at the upper end is attached to the hollow shaft 13.
It is inserted through the seal member 19. The hollow shaft portion 13 is connected to a drive source (not shown),
Further, the hollow rod 18 is fixed to the base 15 and its through hole 20 is connected to the water pump 6. The mold 2 has an opening 7 in one of the holders 32 through the through hole 2.
0 and the mounting flange 17 of the hollow rod 18
Therefore, the mold 2 is held immovably within the tank 5, and the tank 5 is configured to be rotatable around the axis of the mold 2. On the outer periphery of the mold 2, a plurality of rectifying plates 21 extending in the axial direction and radial direction of the mold 2 are arranged at equal intervals in the circumferential direction. The upper end of each rectifying plate 21 is fixed to the annular ceiling surface of a cover 23 covering the tank 5 via an annular mounting plate 22, and the lower end of each rectifying plate 21 is arranged near the bottom of the tank 5. The cover 23 is fixed to the upper surface of the base 15 with a plurality of bolts 24, so that each rectifying plate 21 is immovably disposed around the outer periphery of the mold 2. Between the virtual circle C (FIG. 4) passing through the radially outer surface of the mold 2 of each rectifying plate 21 and the inner peripheral surface of the tank 5,
A plurality of rotating shafts 26 each having a plurality of stirring blades 25 1 in the axial direction are arranged along the circumferential direction of the tank 5 , and a motor 27 for driving each rotating shaft 26 is fixed to the top surface of the cover 23 . In forming the fiber molded body 1, for example, the tank 5 and each stirring blade 251 are rotated clockwise in FIG. 4, and the water pump 6 is operated to apply suction into the mold 2. As a result, near the inner peripheral surface of the tank 5, the tank 5
The flow of the molding material becomes turbulent due to the rotation of the molding material and the stirring action of each stirring blade 25 1 , so that the molding material does not stagnate at the inner bottom of the tank 5 . When the flow of the molding material in a turbulent state collides with each rectifying plate 21, the flow velocity of the flow is weakened, and also because a suction action is applied within the mold 2,
The flow is converted into a laminar flow toward the outer peripheral surface of the mold 2 as shown by the arrow in FIG. This improves the adhesion of the molding material to the mold 2, and the adhered molding material is hardly removed by the flow. Therefore, the production efficiency of the fiber molded body 1 is improved, and the fiber molded body 1 having a uniform thickness can be obtained. Next, an example of the fiber molded body 1 will be described. (a) Preparation of aqueous solution L of molding material Reinforcing fibers with an average diameter of 18 μm and an average length
0.02-0.20% by weight of carbon fibers of 0.8 mm and 0.22-0.40% by weight of alumina fibers with an average diameter of 3-4 μm and an average length of 100-200 μm and 4-6% by weight of silica sol or alumina sol as an inorganic binder.
and 0.2% by weight of the antifoaming agent and surfactant in total, and 93.4 to 95.4% by weight of water (32). The calculated fiber concentration in the tank 5 of the molding material obtained in this way is 4.2 g/Kg.
It is. (b) Dimensions of mold 2 The upper outer diameter is 78 mm, the lower outer diameter is 74 mm, and the thickness is 5 mm. Using the aqueous solution L of the molding material and the mold 2, two types of fiber molded bodies 1 are molded by the apparatus 4 under the conditions shown in the table.
【表】
前記繊維付着率は、
繊維付着率=付着繊維量/濾過水量×繊維濃度×100
より求められる。
従来法により、撹拌羽根の回転数を300520rpm
に設定し、また濾過水量および繊維濃度をそれぞ
れ前記と略同一にして二種類の繊維成形体を形成
し、それらの繊維付着率を求めたところ、撹拌羽
根の回転数300rpmでは94.3%、また回転数
520rpmでは91.8%であり、したがつて本発明方
法により得られた繊維成形体の方が繊維付着率に
おいて優れていることが明らかである。
表は、前記表の条件下(但し、タンク回転
数は40rpm)で成形作業を行つている場合におい
て、各整流板21により囲まれる成形型2外周の
繊維濃度のばらつき状況を示す。[Table] The fiber adhesion rate is determined from: Fiber adhesion rate=Amount of attached fibers/Amount of filtrated water x Fiber concentration x 100. Using the conventional method, the rotation speed of the stirring blade was set to 300,520 rpm.
Two types of fiber molded bodies were formed with the filtration water amount and fiber concentration approximately the same as above, and the fiber adhesion rate was determined. When the stirring blade rotation speed was 300 rpm, it was 94.3%, and the rotation rate was 94.3%. number
At 520 rpm, it was 91.8%, so it is clear that the fiber molded article obtained by the method of the present invention is superior in terms of fiber adhesion rate. The table shows the variation in fiber concentration around the outer periphery of the mold 2 surrounded by each rectifying plate 21 when the molding operation is performed under the conditions shown in the table (however, the tank rotation speed is 40 rpm).
【表】【table】
【表】
表から明らかなように、繊維濃度が最大の部
分と最小の部分との差は0.02g/Kgであり、した
がつて成形型2外周における繊維分布が全体に亘
つて略均一であり、これにより繊維成形体1の厚
さの均一化を達成することができる。
従来法の場合は前記差が0.04g/Kgであり、前
記値の2倍であることが判明している。
第5図は本発明成形方法を実施する成形装置の
他の例を示し、タンク5の内周面に、その母線方
向に延びる複数の撹拌羽根252を円周上等間隔
に設けたものである。
C 発明の効果
本発明によれば、前記のようにタンクの回転、
各撹拌羽根の撹拌作用および各整流板による成形
材料の流れの変換作用により成形材料を十分に撹
拌して成形型外周面に効率良く、且つ均一に付着
させることができ、これにより繊維成形体の生産
能率を向上させると共にその繊維成形体の厚さを
均一にすることができる。[Table] As is clear from the table, the difference between the part with the highest fiber concentration and the part with the lowest fiber concentration is 0.02 g/Kg, which means that the fiber distribution on the outer periphery of the mold 2 is approximately uniform throughout. As a result, the thickness of the fiber molded body 1 can be made uniform. In the case of the conventional method, the above difference is 0.04 g/Kg, which is twice the above value. FIG. 5 shows another example of a molding apparatus for carrying out the molding method of the present invention, in which a plurality of stirring blades 252 extending in the generatrix direction are provided on the inner peripheral surface of the tank 5 at equal intervals on the circumference. be. C. Effects of the Invention According to the present invention, as described above, the rotation of the tank,
Due to the stirring action of each stirring blade and the converting action of the flow of the molding material by each rectifying plate, the molding material can be sufficiently stirred and adhered to the outer circumferential surface of the mold efficiently and uniformly. The production efficiency can be improved and the thickness of the fiber molded article can be made uniform.
第1図は繊維成形体の斜視図、第2図は繊維成
形体の製造工程説明図、第3図は本発明成形方法
を実施する成形装置の縦断正面図、第4図は第3
図−線断面図、第5図は本発明成形方法の実
施に用いられる成形装置の他の例を示す断面図で
第4図に対応する。
L……成形材料の水溶液、2……成形型、5…
…タンク、6……揚水ポンプ、21……整流板、
251,252……撹拌羽根。
FIG. 1 is a perspective view of a fiber molded article, FIG. 2 is an explanatory diagram of the manufacturing process of the fiber molded article, FIG. 3 is a longitudinal sectional front view of a molding apparatus for carrying out the molding method of the present invention, and FIG. 4 is a third
5 is a sectional view showing another example of a molding apparatus used for carrying out the molding method of the present invention, and corresponds to FIG. 4. L...Aqueous solution of molding material, 2...Mold, 5...
... Tank, 6 ... Lifting pump, 21 ... Rectifier plate,
25 1 , 25 2 ... Stirring blade.
Claims (1)
るタンク内に立設された通気性筒状成形型内に吸
引作用を施し、前記成形材料を該成形型の外周面
に付着させて強化用筒状繊維成形体を成形するに
当り、不動に保持された前記成形型の軸線回りに
おける前記タンクの回転および該タンク内周面ま
たはその近傍に存する複数の撹拌羽根の撹拌作用
によりタンク内周面近傍にその周方向に沿う乱流
状態の成形材料の流れを形成し、前記成形型の外
周に配設される複数の整流板に前記成形材料の流
れを衝突させて、該流れを前記成形型の外周面に
向う層流に変換することを特徴とする強化用筒状
繊維成形体の成形方法。1 A suction action is applied to an air-permeable cylindrical mold installed upright in a tank containing an aqueous solution of a molding material containing reinforcing fibers, and the molding material is adhered to the outer peripheral surface of the mold to form a reinforcing cylinder. When molding a fibrous molded product, the rotation of the tank around the axis of the immovably held mold and the stirring action of a plurality of stirring blades existing on or near the inner circumferential surface of the tank cause the inner circumferential surface of the tank to be A turbulent flow of the molding material is formed along the circumferential direction of the mold, and the flow of the molding material collides with a plurality of rectifying plates arranged around the outer periphery of the mold, so that the flow is directed around the mold. A method for forming a reinforcing cylindrical fiber molded body, characterized by converting the flow into a laminar flow toward the outer peripheral surface.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP18318287A JPS6428334A (en) | 1987-07-22 | 1987-07-22 | Formation of cylindrical fiber molding for reinforcement |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP18318287A JPS6428334A (en) | 1987-07-22 | 1987-07-22 | Formation of cylindrical fiber molding for reinforcement |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS6428334A JPS6428334A (en) | 1989-01-30 |
| JPH0428767B2 true JPH0428767B2 (en) | 1992-05-15 |
Family
ID=16131202
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP18318287A Granted JPS6428334A (en) | 1987-07-22 | 1987-07-22 | Formation of cylindrical fiber molding for reinforcement |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS6428334A (en) |
-
1987
- 1987-07-22 JP JP18318287A patent/JPS6428334A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS6428334A (en) | 1989-01-30 |
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