JPH02297425A - Fiber reinforced plastic core stock and core material, and continuous manufacture thereof - Google Patents
Fiber reinforced plastic core stock and core material, and continuous manufacture thereofInfo
- Publication number
- JPH02297425A JPH02297425A JP1117441A JP11744189A JPH02297425A JP H02297425 A JPH02297425 A JP H02297425A JP 1117441 A JP1117441 A JP 1117441A JP 11744189 A JP11744189 A JP 11744189A JP H02297425 A JPH02297425 A JP H02297425A
- Authority
- JP
- Japan
- Prior art keywords
- resin
- sheet
- film
- carrier film
- molded
- 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.)
- Granted
Links
- 239000011162 core material Substances 0.000 title claims abstract description 26
- 238000004519 manufacturing process Methods 0.000 title claims abstract description 15
- 229920002430 Fibre-reinforced plastic Polymers 0.000 title 1
- 239000011151 fibre-reinforced plastic Substances 0.000 title 1
- 229920005989 resin Polymers 0.000 claims abstract description 64
- 239000011347 resin Substances 0.000 claims abstract description 64
- 239000003365 glass fiber Substances 0.000 claims abstract description 30
- 238000000034 method Methods 0.000 claims abstract description 26
- 239000007788 liquid Substances 0.000 claims abstract description 23
- 229920001187 thermosetting polymer Polymers 0.000 claims abstract description 9
- 229920006337 unsaturated polyester resin Polymers 0.000 claims abstract description 5
- 238000000465 moulding Methods 0.000 claims description 23
- 239000011521 glass Substances 0.000 claims description 14
- 239000000463 material Substances 0.000 claims description 12
- 239000004744 fabric Substances 0.000 claims description 9
- 239000000835 fiber Substances 0.000 claims description 8
- 239000011248 coating agent Substances 0.000 claims description 7
- 238000000576 coating method Methods 0.000 claims description 7
- 238000005520 cutting process Methods 0.000 claims description 5
- 238000005507 spraying Methods 0.000 claims description 2
- 238000010030 laminating Methods 0.000 claims 1
- 239000000758 substrate Substances 0.000 claims 1
- 238000005303 weighing Methods 0.000 claims 1
- 238000001723 curing Methods 0.000 description 7
- 238000010438 heat treatment Methods 0.000 description 6
- 239000004033 plastic Substances 0.000 description 4
- 229920003023 plastic Polymers 0.000 description 4
- 229920001225 polyester resin Polymers 0.000 description 4
- 239000004645 polyester resin Substances 0.000 description 4
- 238000009826 distribution Methods 0.000 description 3
- 239000003795 chemical substances by application Substances 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 239000000945 filler Substances 0.000 description 2
- 239000010410 layer Substances 0.000 description 2
- 239000000123 paper Substances 0.000 description 2
- 238000004804 winding Methods 0.000 description 2
- BZHJMEDXRYGGRV-UHFFFAOYSA-N Vinyl chloride Chemical compound ClC=C BZHJMEDXRYGGRV-UHFFFAOYSA-N 0.000 description 1
- 239000000853 adhesive Substances 0.000 description 1
- 230000001070 adhesive effect Effects 0.000 description 1
- 229910052782 aluminium Inorganic materials 0.000 description 1
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 description 1
- 239000011247 coating layer Substances 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 239000003822 epoxy resin Substances 0.000 description 1
- 239000011888 foil Substances 0.000 description 1
- 238000013007 heat curing Methods 0.000 description 1
- 238000005470 impregnation Methods 0.000 description 1
- 238000009776 industrial production Methods 0.000 description 1
- 230000003446 memory effect Effects 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 239000005011 phenolic resin Substances 0.000 description 1
- 229920000647 polyepoxide Polymers 0.000 description 1
- 229920006267 polyester film Polymers 0.000 description 1
- 238000003825 pressing Methods 0.000 description 1
- 238000003303 reheating Methods 0.000 description 1
- 230000003014 reinforcing effect Effects 0.000 description 1
- 238000003860 storage Methods 0.000 description 1
- 229920001169 thermoplastic Polymers 0.000 description 1
- 239000004416 thermosoftening plastic Substances 0.000 description 1
- 229920006305 unsaturated polyester Polymers 0.000 description 1
- 238000009423 ventilation Methods 0.000 description 1
Landscapes
- Moulding By Coating Moulds (AREA)
- Reinforced Plastic Materials (AREA)
- Laminated Bodies (AREA)
Abstract
Description
【発明の詳細な説明】
「産業上の利用分野]
本発明は、FRP、すなわちポリエステル樹脂、エポキ
シ樹脂あるいはフェノール樹脂中に、強化相としてガラ
ス繊11[を混在させて成形したプラスチックを素材に
用い、このものからハニカムコアの中芯用素材ならびに
中芯材を製造する方法に関し、かつこの方法によって製
造した中芯祠を包含する。Detailed Description of the Invention "Field of Industrial Application" The present invention uses FRP, a plastic molded by mixing glass fiber 11 as a reinforcing phase in polyester resin, epoxy resin, or phenol resin, as a material. , relates to a method for manufacturing a honeycomb core core material and a core material from this material, and includes a core mill manufactured by this method.
[従来の技術とその問題点]
プラスチック製のハニカムコアを製造するについては、
例えば特開昭56−98159号公報または米国特許第
2674295号明細書等に開示されているように、従
来から種々の方法が知られているが、いずれも主として
素材シートが柔軟性に富んだ熱可塑性プラスチックを対
象としたものであり、FRPのような熱硬化性樹脂を対
象とする方法は、殆んど知られていない。現実の製品も
、中芯にFRPを用いたものは、本発明者が開発したも
のを除いては、航空機産業でのみ若干使用されているの
みである。それは、素材樹脂が熱硬化性である場合には
、中芯制としての所定の形状を成型、保持さぜることが
容易てなく、したがって、実験室的には製造することは
可能であっても、未だ量産に適した方法は知られていな
いからである。[Conventional technology and its problems] Regarding manufacturing a plastic honeycomb core,
For example, as disclosed in Japanese Patent Application Laid-Open No. 56-98159 or US Pat. This method is intended for plastic plastics, and there are almost no known methods for thermosetting resins such as FRP. In actual products, products using FRP for the core are only slightly used in the aircraft industry, with the exception of the product developed by the present inventor. If the material resin is thermosetting, it is not easy to mold and hold the specified shape as a core, and therefore it is not possible to manufacture it in a laboratory. However, there is still no known method suitable for mass production.
周知のように、FRP製の平板や波板については、技術
的にも既に長い歴史があり、か\るFRP製の平板や波
板が性能の点ても優れた特性を発揮することは広く認識
されている。したがってFRPを中芯に用いたサンドイ
ッチパネルを製造することができれば、非常に高い利用
価値を発揮するもので、それ自体異論のない所であった
が、実際問題として仲々実現しなかった。As is well known, flat plates and corrugated plates made of FRP already have a long technological history, and it is widely known that flat plates and corrugated plates made of FRP exhibit excellent characteristics in terms of performance. Recognized. Therefore, if it were possible to manufacture a sandwich panel using FRP as the core, it would have a very high utility value, and there was no objection to this, but as a practical matter, it was never realized.
ところで、非常に薄いFRPのシートをつくり、それを
ハニカム状にに加工することは、実験室では可能であっ
ても経済的な工業規模で製造するとなると、未解決の問
題が多すぎたというのが現状である。By the way, although it was possible to create extremely thin sheets of FRP and process them into a honeycomb shape in a laboratory, there were too many unresolved problems to manufacture them on an economical industrial scale. is the current situation.
すなわち、一般に、サンドイッチパネルの中芯は、アル
ミ箔や紙、塩ビフィルム等のように最初からシート状に
なっているもので製造される。FRPも薄いシート状の
ものを、あらかじめ製作して、それを中芯に加工する事
も不可能ではない。That is, generally, the core of a sandwich panel is manufactured from a sheet-like material such as aluminum foil, paper, or vinyl chloride film. It is not impossible to make a thin sheet of FRP in advance and process it into a core.
しかし、工程−1−これは二度手間になり、次のような
問題が生じる。つまり、加熱硬化工程は平板で走行させ
ることになるので、非常に長い距離を必要とし、また硬
化した平らなシートを折曲げて蜂の巣状に加工したり、
本発明の場合のような円形(ロールコア状)に加工する
に17ても、再度加熱が必要となるばかりでなく、そも
そもその加工自体が容易ではないのである。However, step-1--this is twice the effort and causes the following problems. In other words, the heat curing process requires a very long distance as it is run on a flat sheet, and the hardened flat sheet must be bent and processed into a honeycomb shape.
Even when processing into a circular shape (roll core shape) as in the case of the present invention, not only is heating required again, but the processing itself is not easy in the first place.
[問題点を解決するための手段]
ここにおいて本発明は、可撓性を備えたキャリヤフィル
ムを連続して繰り出させると共に、このフィルムの表面
に不飽和ポリエステル樹脂等の熱硬化性樹脂の未硬化樹
脂溶液を均一に塗布してから、該塗布液の表面に暴利と
してのガラス繊維を散布または載置した後、その上に別
の可撓性キャリヤフィルムを重ねて走行させると共に、
前記暴利と塗布液とを」二下から圧着脱泡して薄い樹脂
シ一トとなし、さらに、このシートを前記キャリヤフィ
ルムと共に加熱した多数の丸棒に巻き付けて全体が連続
S字形になるように屈曲させた」二で、その形状で成型
硬化させてから、丸棒を離脱した後、前記シートの両面
に配設されたフィルj、をヱ11離するようになし1.
これによって前記した従来法の問題点を解決し得るよう
にしたものである。ちなみに、前記のようにして連続S
字状に成型硬化させた中芯用素材は、これを適宜の長さ
に切断した上で、積層接着させて所要寸法のF RP中
芯+4とするのは勿論である。なおまた、本発明にあっ
ては、前記キャリヤフィルムを剥離した後の成型シート
を成型時に近い温度に再加熱して、連続8字の形状が互
に接触するようにして成型物の修正を連続的に行なうよ
うにした方法をも包含するものである。[Means for Solving the Problems] Here, the present invention continuously unrolls a flexible carrier film, and coats the surface of this film with an uncured thermosetting resin such as an unsaturated polyester resin. After uniformly applying a resin solution, after scattering or placing glass fibers as profiteers on the surface of the coating solution, another flexible carrier film is layered on top of it and run,
The profiteering agent and the coating liquid are pressed and degassed from below to form a thin resin sheet, and this sheet is then wrapped together with the carrier film around a number of heated round rods so that the whole becomes a continuous S-shape. After molding and hardening in that shape, the round rod is removed, and the films arranged on both sides of the sheet are separated by 11 degrees.
This makes it possible to solve the problems of the conventional method described above. By the way, as mentioned above, continuous S
Of course, the material for the core which has been molded and hardened into a character shape is cut to an appropriate length and then laminated and bonded to form an FRP core +4 having the required dimensions. Furthermore, in the present invention, after the carrier film has been peeled off, the molded sheet is reheated to a temperature close to that at the time of molding, so that the continuous figure 8 shapes are brought into contact with each other to continuously correct the molded product. It also includes methods that are carried out on a regular basis.
さらにまた、前記基オAとしてのガラス繊維は、これを
短寸にカットしたものでも、或いはガラスクロスの何れ
でもよく、さらにまた、薄くかっl」の粗いガラスクロ
スを用いたときには、交差した繊維と繊維の間に樹脂の
欠落部を形成させることができるので、それによって成
型後の樹脂シートの全面に対し均一にピンホールを形成
させることができる。なお、暴利としてガラスチョップ
を用い、ると共に、そのガラスチョップの散布量とキャ
リヤフィルムの表面に塗布する樹脂量との間において、
塗布する樹脂量よりもガラス繊維の散布比率を高くした
場合には、それによっても成型後の樹脂シフト全域に均
一なピンホールを形成させることができる。Furthermore, the glass fiber as the group A may be either one cut into short pieces or a glass cloth. Furthermore, when a thin and coarse glass cloth is used, the crossed fibers may be used. Since missing portions of the resin can be formed between the resin sheet and the fibers, pinholes can be uniformly formed over the entire surface of the resin sheet after molding. In addition, when a glass chop is used as a profiteer, the difference between the amount of spraying of the glass chop and the amount of resin applied to the surface of the carrier film is
When the glass fiber distribution ratio is higher than the amount of resin applied, uniform pinholes can be formed in the entire resin shift area after molding.
前述のように、本発明によれば、不定形の液状樹脂とガ
ラス繊維とを硬化前に必要な形状に成型してしまう方法
を提供するものであるから、極めて能率的な方法であっ
て、しかも、−挙に連続8字の成型シートが得られるか
ら、これを平板から加工してゆく場合に比較して、約1
15の距離スペースで足りるという利点を発揮する。ま
た、樹脂を硬化させるには加熱を必要とするが、その加
熱に用いる炉の長さも平板をつくる場合に較べ短くて済
むので、大幅に能率を挙げることができる。As described above, the present invention provides a method of molding an amorphous liquid resin and glass fiber into a required shape before curing, which is an extremely efficient method. Moreover, since a molded sheet with 8 consecutive characters can be obtained at once, compared to processing it from a flat plate, it is about 1.
This has the advantage that 15 distance spaces are sufficient. Furthermore, although heating is required to cure the resin, the length of the furnace used for heating is shorter than that required for making flat plates, so efficiency can be greatly improved.
ちなみに、成型後の樹脂シートに対し積極的にピンホー
ルを形成させる場合は別にして、ピンホールを作らずに
、出来るだけ薄いシートを形成させる場合には、樹脂量
で0.2〜0.4 kg/r+f、ガラス繊維量で0.
1〜0.2 Kg/m2’の範囲とするのを可とする。By the way, apart from the case where pinholes are actively formed in the resin sheet after molding, when forming a sheet as thin as possible without forming pinholes, the amount of resin is 0.2 to 0. 4 kg/r+f, glass fiber amount 0.
A range of 1 to 0.2 Kg/m2' is acceptable.
[実施態様] 以下、本発明を図示の装置に基づき具体的に説明する。[Embodiment] Hereinafter, the present invention will be specifically explained based on the illustrated apparatus.
第1図において、符号1はギヤリヤフィルムであって、
無機質または何機質を問わず、耐熱性を有する可撓性の
フィルムであれは、すべて用いることができ、紙、金属
、熱可塑性、熱硬化性樹脂フィルムのいずれでもよい。In FIG. 1, numeral 1 is a gear rear film,
Regardless of whether it is inorganic or organic, any heat-resistant and flexible film can be used, including paper, metal, thermoplastic, and thermosetting resin films.
しかして、前記キャリヤフィルムの巻取1.aより繰り
出させた帯状のフィルム1を、未硬化状態にある熱硬化
性樹脂の溶液を満たした貯槽2内に浸漬回転する塗布ロ
ール3に接触させて、走行するフィルム1の表面に、−
例として不飽和ポリエステルの樹脂溶液4を、所定の塗
布量となるように均一に塗布する。Thus, winding of the carrier film 1. The strip-shaped film 1 let out from a is immersed in a storage tank 2 filled with a solution of an uncured thermosetting resin and brought into contact with a rotating application roll 3 to coat the surface of the running film 1 with -
For example, a resin solution 4 of unsaturated polyester is uniformly applied to a predetermined amount.
次いで、該樹脂液の上に、−例として短(」°にカソト
したガラス繊維5を均一に散布するか、もしくは平織り
としたガラス繊維を連続的に載置してゆく。第1図中、
符号6はガラス長繊維の巻取、7は前記長繊維を短寸に
カットするための裁断装置、同8はホッパである。ガラ
ス繊維5が散布または配設された樹脂液4は、キャリヤ
フィルム1と共に同図に示すように右方に走行し、つい
でさらに、その上に前記と同様な構成のキャリヤフィル
ム9が、巻取9aを介して繰り出されて、前記樹脂液の
」二面にかぶさるようにラミネートさせる。かくして当
該樹脂液は、ガラス繊維と共に上下側面からキャリヤフ
ィルム1および9に挟みこまれた状態(この状態を符号
]0で示す)となる。この状態のまま、ニップロール1
1.11の間に導いて前記樹脂液を圧着、脱泡した上で
、次段の成形装置12に導入する。以下、前記成型装置
の一例を、第1図に基いて具体的に説明する。同図にお
いて、上下一対の無端状チェノ20.21を」1下対称
に懸張し、かつこれらチェノに対し、多数の丸棒22,
23を回転自在に装着する。しかして前記チェノ20,
21が図示を省略したチェンポイルの駆動に伴って案内
板24.25の間に導かれて走行すると、それに随伴し
て上下の各チェノに取りイ」けられた丸棒22と23と
が上下から噛み合うようにして互い違いに係合しあった
状態で運行する。なお、図に符号26で示すように、前
記各装置の全体を一つの筐体内に収納するようになし、
かつ該筐体26の内部には一例として赤外線ランプ27
を取りト1けて、前記丸棒22,23を加熱し得るよう
にしておく。Next, on top of the resin liquid, glass fibers 5 cut short (for example) are uniformly scattered, or plain-woven glass fibers are continuously placed.
Reference numeral 6 is a winding device for the long glass fibers, 7 is a cutting device for cutting the long fibers into short pieces, and 8 is a hopper. The resin liquid 4 on which the glass fibers 5 are scattered or disposed travels together with the carrier film 1 to the right as shown in the figure, and then a carrier film 9 having the same structure as described above is further rolled up. 9a and laminated so as to cover both sides of the resin liquid. In this way, the resin liquid and the glass fibers are sandwiched between the carrier films 1 and 9 from the upper and lower sides (this state is indicated by the symbol 0). In this state, nip roll 1
1.11, the resin liquid is compressed and degassed, and then introduced into the next molding device 12. Hereinafter, an example of the molding apparatus will be specifically explained based on FIG. 1. In the figure, a pair of upper and lower endless chinos 20 and 21 are suspended symmetrically by 1", and a large number of round bars 22,
23 is attached rotatably. However, the Cheno 20,
When 21 is guided between the guide plates 24 and 25 by the drive of a chain poil (not shown), the round bars 22 and 23, which are attached to the upper and lower chains, are moved from above and below. They operate in a state where they are engaged with each other alternately. In addition, as shown by the reference numeral 26 in the figure, each of the above-mentioned devices is housed in a single housing,
In addition, an infrared lamp 27 is provided inside the housing 26, as an example.
The round rods 22 and 23 are heated so that they can be heated.
ところで、前記成型装置12における成型用丸棒23.
24の加熱温度は、使用する熱硬化樹脂の硬化温度によ
っても異なるが、好ましくは、100°C程度に加熱し
ておき、この加熱丸棒に前記した樹脂液の層状物をその
両面からキャリヤフィルムをあてがった状態で、キャリ
ヤフィルム毎(符号10参照)丸棒に巻きつけて接触さ
せ、連続S字形に成型する。符号10で示される樹脂液
の層状物は、前記丸棒22と23とが係合しあったまま
移行する間に硬化し、FRPの非常に薄い成型シートと
なる。By the way, the molding round bar 23 in the molding device 12.
The heating temperature in step 24 varies depending on the curing temperature of the thermosetting resin used, but it is preferably heated to about 100°C, and the above-mentioned resin liquid layer is applied to this heated round bar from both sides of the carrier film. With the carrier film applied, each carrier film (see reference numeral 10) is wound around a round bar and brought into contact with it to form a continuous S-shape. The layered resin liquid indicated by the reference numeral 10 hardens while the round rods 22 and 23 move while being engaged with each other, and becomes a very thin molded sheet of FRP.
その状態は、第2図に示すとおりであって、丸棒を抱え
込んだ状態で硬化した連続S字形の成型シート13は、
キャリヤフィルム1および9をラミネートしたままS字
形に成型されるが、この状態から丸棒22または23が
抜は出す際には、第2図に示すように、フィルムおよび
シートの全体がU字形に開くように変形する。すなわち
、丸棒22.24は、成型後のシートら抜は出すように
外されて、成型装置から排出される。ちなみに、上記の
ようにして丸棒が外された成型物シート13は、弾性が
あるので完全ではないが、はぼ元の形状に戻り連続8字
の形を維持する。The state is as shown in FIG. 2, and the continuous S-shaped molded sheet 13 that has hardened while holding the round bar is
The laminated carrier films 1 and 9 are formed into an S-shape, but when the round bar 22 or 23 is removed from this state, the entire film and sheet form a U-shape as shown in FIG. Transform to open. That is, the round bars 22, 24 are removed from the sheet after molding and are discharged from the molding apparatus. Incidentally, the molded sheet 13 from which the round bars have been removed as described above is elastic, so although it is not perfect, it returns to its original shape and maintains the continuous figure eight shape.
上記のように本発明においては、前記樹脂液をキャリヤ
フィルム上において、層状に塗布形成させてから、これ
を−例として概ね100℃前後の温度下に加熱硬化させ
るものであって、この場合の温度設定については次の点
を考慮する必要がある。As mentioned above, in the present invention, the resin liquid is coated and formed in a layer on a carrier film, and then heated and cured at a temperature of about 100°C, for example. Regarding temperature settings, the following points need to be considered.
すなわち、比較的薄いFRPシートを高温の丸棒に直接
接触させると、温度の伝達が早くポエステル樹脂は急激
な温度上昇により極端な粘度低下をきたすと共に、丸棒
に巻きつけたときのフィルムとの接触圧によって、フィ
ルムの両縁部から樹脂やガラス繊維が、はみ出してしま
う虞れがある。In other words, when a relatively thin FRP sheet is brought into direct contact with a hot round rod, the temperature transfers rapidly, and the polyester resin experiences an extreme drop in viscosity due to the rapid temperature rise, and the viscosity of the polyester resin decreases when it is wrapped around the rod. Due to the contact pressure, there is a risk that the resin or glass fibers may protrude from both edges of the film.
そこで、実施に際しては、この粘度低下を防ぐために、
エロジールなどの充填剤を添加するとよい。Therefore, in order to prevent this viscosity reduction, when implementing
A filler such as Erosil may be added.
なお、常温での粘度が高くなりすぎると、ガラス繊維へ
の含浸や脱泡力哨1゜しくなるので、この点についても
配慮する必要がある。Note that if the viscosity at room temperature becomes too high, impregnation into glass fibers and defoaming will become difficult, so this point also needs to be taken into consideration.
これを要するに、樹脂液がキャリヤフィルムの縁部より
流出するのを防ぎ、同時に硬化速度を早め得るように充
填剤を配合した」二で、概ね100°C前後の硬化温度
で装置を運用するようにするのが最も適当である。また
、連続S字形に組合わさった丸棒を、FRPシートと共
に進行させて加熱状態を保つと、それら丸棒に咬え込ま
れたポリエステル樹脂は、添加された硬化剤の種類、配
合量にもよるが、約2分程で硬化する。硬化が終了した
後、前述のように丸棒は成型シートからはずされ、もと
に戻って再び新しいシートが巻きつけられて硬化が行わ
れるもので、前記のようにして繰返しの作業が連続的に
遂行される。前述のように、本発明においては樹脂シー
トを成型硬化した後に、成型の用に供した丸棒を該シー
トから取り外すのであるが、成型樹脂シートは、硬化後
にあっても、未だその時点では100℃の温度になって
いるので多少軟化状態にあり、したがって、引き抜きに
支障を生ずることはない。なお、加温した状態で丸棒を
引き抜いた後のシートの形状は、完全なS字形に戻らず
、第2図に符号Aで示すような隙間が生ずる。これに反
し、前記シートと丸棒を完全に冷却した後、常温下で丸
棒をはずすと、FRPの弾性によって、第4図のように
完全に元(ミ復する。In short, we added a filler to prevent the resin liquid from flowing out from the edges of the carrier film and at the same time speed up the curing speed. It is most appropriate to do so. In addition, when the round bars combined in a continuous S-shape are advanced together with the FRP sheet and maintained in a heated state, the polyester resin bitten by the round bars will change depending on the type and amount of the curing agent added. It will harden in about 2 minutes, but it will harden in about 2 minutes. After curing is completed, the round bar is removed from the molded sheet as described above, returned to its original position, and a new sheet is wrapped around it again for curing. will be carried out. As mentioned above, in the present invention, after the resin sheet is molded and hardened, the round rod used for molding is removed from the sheet, but even after the molded resin sheet is hardened, it still has a 100% ℃, so it is in a somewhat softened state, so there is no problem in drawing it out. Note that the shape of the sheet after the round rod is pulled out in a heated state does not return to a perfect S-shape, and a gap as shown by symbol A in FIG. 2 is generated. On the other hand, when the sheet and round bar are completely cooled and the round bar is removed at room temperature, the elasticity of FRP completely restores the original shape as shown in Figure 4.
しかし、加温下に丸棒を外した場合において、若干形が
歪んだとしても、それについては、後記のようにして修
正を行えばよい。However, even if the shape is slightly distorted when the round bar is removed while being heated, it can be corrected as described below.
上記のようにして成型されたシートは、第1図に示すよ
うに、コンベヤ1.4を介して後段に送られ、該コンベ
ヤの末端部に取りイ」けられた剥離治具15により、不
要となったキャリヤフィルムのみが該成型シートの両面
から引き剥がされる(第3図参照)。なお、引き剥がさ
れた各フィルムは、それぞれ巻取り1.aならびに9b
として巻取られてゆく。As shown in FIG. 1, the sheet formed in the above manner is sent to a later stage via a conveyor 1.4, and is removed by a peeling jig 15 installed at the end of the conveyor. Only the carrier film, which has become , is peeled off from both sides of the molded sheet (see FIG. 3). Note that each peeled film is wound up in 1. a and 9b
It is wound up as.
すなわち、丸棒22,23から脱型された後は、両面に
キャリヤフィルム1および9が被覆された状態のFRP
シート13が進行していくので、前記成型装置の後段に
は、このフィルムを剥離する工程を設ける。この場合、
該シート13は、未だ高い温度にあり、この状態では非
常に剥離しにくい。それは、FRPのシートが薄く、軟
化しているため僅かの力で変形してしまうからであり、
したがって、ある程度、冷却してから剥離するのがよい
。また、比較的薄い連続S字形の成型シートを対象とし
て剥離させる場合、第3図のX個所は180°剥離で剥
がし易いが、yの個所は成型シートとほとんど平行であ
るため、成型品が変形して90°近くになるまで剥離は
しない。また、剥離した両面のフィルムを一定速度で巻
取っても、剥離力の強弱が間欠的に起こり、それが両側
で生じるので、激しい振動が起こる虞れがある。かかる
不具合を防ぐために、図示のような剥離治具15を用い
るのを可とする。That is, after being demolded from the round bars 22 and 23, the FRP is coated with carrier films 1 and 9 on both sides.
As the sheet 13 progresses, a step for peeling off this film is provided at a subsequent stage of the molding device. in this case,
The sheet 13 is still at a high temperature and is very difficult to peel off in this state. This is because FRP sheets are thin and softened, so they deform with the slightest force.
Therefore, it is better to cool it down to some extent before peeling it off. In addition, when peeling a relatively thin continuous S-shaped molded sheet, the X location in Figure 3 is easy to peel off by 180° peeling, but the y location is almost parallel to the molded sheet, so the molded product is deformed. Do not peel until the angle is close to 90°. Furthermore, even if the peeled film on both sides is wound up at a constant speed, the strength of the peeling force will intermittently change, and this will occur on both sides, which may cause severe vibrations. In order to prevent such problems, it is possible to use a peeling jig 15 as shown.
ところで、」1記実施例においては、前記のようにして
キャリヤフィルムを剥離した後の成型シート13をヒー
タJ6に導き、ここで成型時に近い温度で再加熱するよ
うな工程を付加したものである。By the way, in Example 1, a step was added in which the molded sheet 13 after the carrier film was peeled off as described above was guided to the heater J6, where it was reheated at a temperature close to that of molding. .
この様な操作を加えると、成型された樹脂シートは、一
種の形状記憶作用によって成型時の、すなわち隣り合う
S字形が互いに接触した状態での歪みのない連続S字形
状に修正されるから、好ましくは、この加熱工程を付加
するのがよい。かくして得られた連続S字形の成型シー
ト13は、切断装置J7によって必要な長さしに切断さ
れて(第4図参照)、いわゆる中芯用の素材とするもの
である。When such an operation is applied, the molded resin sheet is corrected to a continuous S-shape without distortion due to a kind of shape memory effect, that is, when adjacent S-shapes are in contact with each other, Preferably, this heating step is added. The continuous S-shaped molded sheet 13 thus obtained is cut into required lengths by a cutting device J7 (see FIG. 4), and is used as a material for a so-called core.
」1記のようにしてFRPだけで構成された中芯素材た
る成型シート13を、一定長さに切断して第4図に示す
ような製品とし、さらにこのものに接着剤を塗布して積
層、圧締、加熱硬化して接着を完了させると、第5図に
示すようにな積層品かえられる。そこで、これを例えば
バンドソーなどで適当な高さHを保持するように切断す
れば、第6図に示すようなFRP中芯利が完成する。The molded sheet 13, which is the core material made only of FRP, is cut into a certain length as described in 1 above to produce a product as shown in Fig. 4, which is then coated with adhesive and laminated. After completion of adhesion by pressing, heating and curing, a laminated product as shown in FIG. 5 is obtained. Then, if this is cut using a band saw or the like to maintain an appropriate height H, an FRP core as shown in FIG. 6 will be completed.
実施例1
キャリヤフィルムとしてフィルム幅が500 mmのポ
リエステルフィルム(30μ厚)を、10m/mJnの
速度で走行させ、それに不飽和ポリエステル樹脂液を0
.20kg/m2になるように塗布し、その塗布面にガ
ラス繊維のストランドを長さ30mmにカットしたもの
を0.1. kg/ryl’になるよう散布した。その
上に、さらに前述と同じフィルムを供給した前記したガ
ラス繊維の散布面を上下両面からキャリヤフィルムで挾
みつけて走行させ、かつローラで圧着し、脱泡する。そ
れを温度100°Cに加熱した直径8.5 mm、長さ
520 mmの丸棒に連続S字形に巻きつけて成型、硬
化させた。丸棒の連結長さは、2mであり、キャリヤフ
ィルムを剥離した後のFRPシートの8字部分の開きは
、約3mmであった。Example 1 A polyester film (30μ thick) with a film width of 500 mm was run as a carrier film at a speed of 10 m/mJn, and an unsaturated polyester resin liquid was added to it at 0.
.. A glass fiber strand cut to a length of 30 mm was coated on the coated surface at a weight of 20 kg/m2. It was sprayed at a rate of kg/ryl'. On top of that, the same film as described above is further supplied, and the above-mentioned glass fiber distribution surface is sandwiched between upper and lower surfaces by carrier films and run, and is pressed with a roller to defoam. It was heated to 100°C and wound around a round bar with a diameter of 8.5 mm and a length of 520 mm in a continuous S-shape, and was molded and cured. The connecting length of the round rods was 2 m, and the opening of the figure 8 portion of the FRP sheet after peeling off the carrier film was about 3 mm.
これを100°Cに加熱、冷却して成型後の形状を修正
し、このときの成型速度は2 m / m ]、nであ
った。This was heated to 100°C and cooled to correct the shape after molding, and the molding speed at this time was 2 m/m], n.
また、このようにして得られたFRPシートを積層接着
したときの見かけ密度は、100kg/m3であった。Further, the apparent density when the FRP sheets obtained in this manner were laminated and bonded was 100 kg/m3.
このブロックを、20mm厚さに切断して、圧縮強度を
測定すると、80kg/cm2であった。This block was cut to a thickness of 20 mm and the compressive strength was measured to be 80 kg/cm2.
実施例2
丸棒の径を14mmとした以外は、上記と同じ方法で中
芯材を得た。樹脂量は、0.3 kg/rd、ガラス繊
維量は、0.15kg/m2であった。また、製品の見
かけ密度は120 kg/m”であった。このときの圧
縮強度は100kg/cm2であった。Example 2 A core material was obtained in the same manner as above except that the diameter of the round bar was 14 mm. The amount of resin was 0.3 kg/rd, and the amount of glass fiber was 0.15 kg/m2. Further, the apparent density of the product was 120 kg/m''. The compressive strength at this time was 100 kg/cm2.
実施例3 」1記と同じ方法にて、丸棒の径を231とじた。Example 3 ” The diameter of the round bar was cut to 231 using the same method as in 1.
樹脂量は0.4kg/m2’、ガラス繊維量は0.2k
g/n−rとしたときの製品の見かけ密度は、80kg
/y11”であった。このときの圧縮強度は80 kg
/cm2であった。The amount of resin is 0.4kg/m2', the amount of glass fiber is 0.2k
The apparent density of the product when g/n-r is 80 kg
/y11”.The compressive strength at this time was 80 kg
/cm2.
実施例4
実施例2と同じ方法で、ガラス繊維のみ144g/rd
の平織ガラスクロスとした。なお、このクロスは25m
m幅で、タテ糸およびヨコ糸がそれぞれ19本であった
。また、見かけ密度は1.20 kg/m”、圧縮強度
は、105kg/cm2であった。この製品には、0.
1 mmφ程度のピンポールが、成型シート面全域に均
一に生じていた。Example 4 Same method as Example 2, only glass fiber 144g/rd
Made of plain woven glass cloth. In addition, this cross is 25m
m width, and there were 19 warp threads and 19 weft threads each. In addition, the apparent density was 1.20 kg/m'' and the compressive strength was 105 kg/cm2.
Pin poles of about 1 mmφ were uniformly generated over the entire surface of the molded sheet.
以」二に詳述したように、本発明によると、FRPシー
トの厚さは、これをキャリヤフィルム−七に塗布形成す
る樹脂液の塗布量によって制御し得る。As described in detail below, according to the present invention, the thickness of the FRP sheet can be controlled by the amount of resin liquid applied to the carrier film 7.
したかって、かなり薄いものを製造し得るはがりでなく
、成型シート面全域に積極的にピンホールを生じさせる
ことも可能である。Therefore, it is possible to actively create pinholes over the entire surface of the molded sheet, rather than using peeling that can produce a fairly thin sheet.
ちなみに、ピンホールをつくらずに、できるだけ薄いシ
ートをっくるには、樹脂量で0.2〜0.4kg/イ、
ガラス繊維量で0.1〜0.2kg/m2の範囲とする
のがよい。By the way, in order to make a sheet as thin as possible without creating pinholes, the amount of resin should be 0.2 to 0.4 kg/i,
The amount of glass fiber is preferably in the range of 0.1 to 0.2 kg/m2.
サンドイッチパネルの中芯利として、用途によっては、
通気性を備えているのがよい場合もある。Depending on the application, it can be used as the center core of sandwich panels.
In some cases, it is good to have ventilation.
この場合には、前記実施例4で示すようにガラスクロス
を用いれはよく、この場合、暴利としてl」の粗いガラ
スクロスを使用すると、繊維の部分だけに樹脂が固まっ
て、交差した繊維と繊維の間には樹脂の欠落部ができ、
それによって非常に均一なピンポールを全面に形成させ
ることができる。In this case, glass cloth may be used as shown in Example 4. In this case, if a coarse glass cloth of 1" is used for profiteering, the resin will harden only on the fibers and the crossed fibers will There is a gap in the resin between the
This allows very uniform pinpoles to be formed over the entire surface.
なお、前記カラスクロスに代えてガラスチョップを用い
ても、それを製作することかできる。太きなピンポール
を形成させるには、できるだけ薄いシートにすることと
、塗布する樹脂量よりもガラス繊維の散布比率を高くず
れはよい。Note that it is also possible to manufacture a glass chopper instead of the crow cloth. In order to form thick pin poles, it is best to make the sheet as thin as possible and to set the glass fiber distribution ratio higher than the amount of resin applied.
[発明の効果]
本発明によれは、従来、困難視されていたFRP中芯祠
を極めて安価に製造することができ、しかも、断面ロー
ルコア状のFRPシートを連続的に製造することが出来
る点で、新規なる工業的効果を有する。また、本発明に
よれば、屈曲した中芯祠を平板から加工の」二で製造す
るのでなしに、最初からS字形に成型、硬化させて製造
するようにしたから製造に要する機械装置が占める床面
積も、炉の長さを含め、平板のそれに較べて格段に少な
くすることができる。[Effects of the Invention] According to the present invention, it is possible to manufacture an FRP core shrine at an extremely low cost, which was considered difficult in the past, and furthermore, it is possible to continuously manufacture an FRP sheet having a rolled core shape in cross section. This has new industrial effects. In addition, according to the present invention, instead of manufacturing the bent core shrine from a flat plate in two steps, it is manufactured by molding it into an S-shape from the beginning and hardening it, so that the mechanical equipment required for manufacturing is occupied. The floor space, including the length of the furnace, can also be significantly reduced compared to that of a flat plate.
このように、本発明は、連続S字形のFRPシートを実
験室規模から工業生産にまで高め、安価なFRP中芯の
提供を可能ならしめた点において極めて有意義なもので
ある。As described above, the present invention is extremely significant in that it has enabled continuous S-shaped FRP sheets to be produced from a laboratory scale to industrial production, and it has made it possible to provide an inexpensive FRP core.
第1図は、本方法を実施する場合の一例を示す工程全体
の説明図、第2図は、成型後のシートから成型用丸棒を
引き抜く状態を示した断面図、第3図は成型シートから
キャリヤフィルムを剥離する状態を示した説明図、第4
図は、本方法によって製造された中芯用素材の外観を示
す斜視図、第5図および第6図は、本発明によって得ら
れる製品の外観を示す斜視図である。
1.9:キャリヤフィルム、 2:樹脂溶液、3:塗布
ロール、 4:樹脂液の塗布層、5:短寸のガラス繊維
、 7:裁断装置、11:ニップロール、 12:成型
装置、13:成型後の樹脂シート、 14:コンベヤ、
15:剥離冶具、16:再加熱装置、17:カッタ、2
2.23 :成型用丸棒、24.25 :案内板、26
:筐体、27:加熱ランプ、
第2図
第4図
第3図
第6図
第5図Fig. 1 is an explanatory diagram of the entire process showing an example of carrying out this method, Fig. 2 is a sectional view showing a state in which a round bar for forming is pulled out from a sheet after forming, and Fig. 3 is a formed sheet. Explanatory diagram showing the state in which the carrier film is peeled off from the
The figure is a perspective view showing the appearance of the core material produced by the method of the present invention, and FIGS. 5 and 6 are perspective views showing the appearance of the product obtained by the invention. 1.9: carrier film, 2: resin solution, 3: coating roll, 4: coating layer of resin liquid, 5: short glass fiber, 7: cutting device, 11: nip roll, 12: molding device, 13: molding rear resin sheet, 14: conveyor, 15: peeling jig, 16: reheating device, 17: cutter, 2
2.23: Round bar for molding, 24.25: Guide plate, 26
: Housing, 27: Heat lamp, Figure 2 Figure 4 Figure 3 Figure 6 Figure 5
Claims (1)
させ、かつ、このフィルムの表面に熱硬化性樹脂の未硬
化樹脂溶液を均一に塗布してから該塗布液の表面に基材
としてのガラス繊維を散布または載置した後、その上に
別の可撓性キャリヤフィルムを重ねて走行させると共に
、前記基材と塗布液とを上下から圧着脱泡して薄い樹脂
シートとなし、さらに、このシートを前記キャリヤフィ
ルムと共に加熱した多数の丸棒に巻き付けて全体が連続
S字形になるように屈曲させた上で、その形状で成型硬
化させてから、丸棒を離脱した後、前記シートの両面に
配設されたフィルムを剥離して成る中芯用素材の製造法
。 2 連続して流れるキャリヤフィルムの上に、不飽和ポ
リエステル樹脂液を均一に塗布した後、該樹脂液の表面
に短寸にカットしたガラス繊維を均一に散布するか、ま
たはガラスクロスを配設した後、さらにこの上にキャリ
ヤフィルムを重ねて走行させ、さらに前記樹脂液を圧着
脱泡することによって比較的薄い樹脂シート層を形成す
る第一工程と、このシート層を、加熱した多数の丸棒が
互い違いに係合したまま進行する成型装置に導き、前記
丸棒に対して前記の樹脂シート層をキャリヤフィルムご
と連続S字形になるように巻きつけた状態で成型硬化さ
せてから、丸棒を離脱させる第二工程と、前記樹脂シー
ト層の両面に配設されたキャリヤフィルムを該シート層
から引き剥がす第三工程と、さらに前記のようにして成
型硬化した樹脂シート層を所要長さに切断した上で、そ
れらを積層接着してなる第四工程とを組み合わせたこと
を特徴とするFRP中芯材の製造法。 3 未硬化樹脂溶液としての不飽和ポリエステル樹樹脂
の量を0.2〜0.4kg/m^2とした請求第1〜2
項のいずれかに記載の方法。 4 基材としてのガラス繊維量を0.1〜0.2kg/
m^2とした請求第1〜3項のいずれかに記載の方法。 5 ガラス繊維が0.1〜0.2kg/m^2の平織と
したガラスクロスである請求第1〜4項のいずれかに記
載の方法。 6 成型用丸棒の温度を80〜120℃でほぼ一定温度
に保ち、それを循環使用する請求第1〜5項のいずれか
に記載の方法。 7 フィルムの剥離は、成型シートの温度を50℃以下
に保持し、かつ剥離治具を使用して行なう請求第1〜6
項のいずれかに記載の方法。 8 フィルムの剥離後、成型シートを成型時に近い温度
に再加熱して、連続S字の形状が互に接触するようにし
て成型物の修正を連続して行なう請求第1〜7項のいず
れかに記載の方法。 9 基材として目の粗いガラスクロスを使用して交差し
た繊維と繊維の間に樹脂の欠落部を形成させ、それによ
って均一なピンホールを全面に形成させるようにした請
求第1〜8項記載の方法。 10 基材としてガラスチョップを用い、かつそのガラ
スチョップの散布量とキャリヤフィルムの表面に塗布す
る樹脂量との間において、塗布する樹脂量よりもガラス
繊維の散布比率を高くすることによって成型後の樹脂シ
ートの全域に均一なピンホールを形成させるようにした
請求第1〜8項記載の方法。 11 可撓性を備えたキャリヤフィルムを連続して繰り
出させ、かつ、このフィルムの表面に熱硬化性樹脂の未
硬化樹脂溶液を均一に塗布してから該塗布液の表面に基
材としてのガラス繊維を散布または載置した後、その上
に別の可撓性キャリヤフィルムを重ねて走行させると共
に、前記基材と塗布液とを上下から圧着脱泡して薄い樹
脂シートとなし、さらに、このシートを前記キャリヤフ
ィルムと共に加熱した多数の丸棒に巻き付けて全体が連
続S字形になるように屈曲させた上で、その形状で成型
硬化させてから、丸棒を離脱した後、前記シートの両面
に配設されたフィルムを剥離して製造した樹脂シートを
所要長さに切断した上で、それらを積層接着してなるF
RP中芯材。[Scope of Claims] 1. A flexible carrier film is continuously fed out, and an uncured resin solution of a thermosetting resin is uniformly applied to the surface of the film, and then the surface of the coating liquid is applied. After scattering or placing glass fiber as a base material on the substrate, another flexible carrier film is layered on top of the glass fiber and the coating liquid is pressed and degassed from above and below to form a thin resin sheet. Furthermore, this sheet was wrapped around a number of heated round bars together with the carrier film, the whole was bent so as to form a continuous S-shape, the sheet was molded and cured in that shape, and then the round bars were separated. Then, the method for producing a core material is performed by peeling off the films disposed on both sides of the sheet. 2. After uniformly applying an unsaturated polyester resin liquid onto a continuously flowing carrier film, glass fibers cut into short lengths were uniformly sprinkled on the surface of the resin liquid, or glass cloth was placed on the surface of the resin liquid. After that, a carrier film is layered on top of this and run, and the resin liquid is pressed and degassed to form a relatively thin resin sheet layer.This sheet layer is then passed through a number of heated round rods. The resin sheet layer and the carrier film are wrapped around the round bar in a continuous S-shape, and the round bar is molded and cured. a second step of separating the resin sheet layer; a third step of peeling off the carrier film disposed on both sides of the resin sheet layer from the sheet layer; and further cutting the molded and cured resin sheet layer to a required length. A method for manufacturing an FRP core material, characterized in that the fourth step of laminating and adhering them is combined. 3 Claims 1 to 2 in which the amount of unsaturated polyester resin as an uncured resin solution is 0.2 to 0.4 kg/m^2
The method described in any of the paragraphs. 4 The amount of glass fiber as the base material is 0.1 to 0.2 kg/
The method according to any one of claims 1 to 3, wherein m^2. 5. The method according to any one of claims 1 to 4, wherein the glass fiber is a plain weave glass cloth weighing 0.1 to 0.2 kg/m^2. 6. The method according to any one of claims 1 to 5, wherein the temperature of the molding round bar is maintained at a substantially constant temperature of 80 to 120°C and used cyclically. 7. The peeling of the film is carried out by keeping the temperature of the molded sheet below 50°C and using a peeling jig.
The method described in any of the paragraphs. 8. After peeling off the film, the molded sheet is reheated to a temperature close to that during molding, and the molded product is continuously corrected so that the continuous S-shaped shapes are in contact with each other. The method described in. 9. Claims 1 to 8, wherein a coarse glass cloth is used as the base material and resin gaps are formed between the crossed fibers, thereby forming uniform pinholes over the entire surface. the method of. 10 By using a glass chop as a base material and making the spraying ratio of glass fiber higher than the amount of resin to be applied between the amount of the glass chop and the amount of resin applied to the surface of the carrier film, the 9. The method according to claim 1, wherein uniform pinholes are formed over the entire area of the resin sheet. 11 A flexible carrier film is continuously fed out, and an uncured resin solution of a thermosetting resin is uniformly applied to the surface of this film, and then glass as a base material is applied to the surface of the coating solution. After scattering or placing the fibers, another flexible carrier film is layered on top of the fibers and run, and the base material and the coating liquid are pressed and degassed from above and below to form a thin resin sheet. The sheet is wrapped around a number of heated round rods together with the carrier film, bent so that the entire sheet forms a continuous S-shape, and then molded and cured in that shape. After the round rods are removed, both sides of the sheet are bent. A resin sheet produced by peeling off the film placed on the film is cut to the required length, and then laminated and bonded to form an F.
RP core material.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP1117441A JPH02297425A (en) | 1989-05-12 | 1989-05-12 | Fiber reinforced plastic core stock and core material, and continuous manufacture thereof |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP1117441A JPH02297425A (en) | 1989-05-12 | 1989-05-12 | Fiber reinforced plastic core stock and core material, and continuous manufacture thereof |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH02297425A true JPH02297425A (en) | 1990-12-07 |
JPH0567415B2 JPH0567415B2 (en) | 1993-09-24 |
Family
ID=14711727
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP1117441A Granted JPH02297425A (en) | 1989-05-12 | 1989-05-12 | Fiber reinforced plastic core stock and core material, and continuous manufacture thereof |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH02297425A (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH04249542A (en) * | 1990-12-19 | 1992-09-04 | Matsushita Electric Works Ltd | Production of thin smc sheet |
JP2016199996A (en) * | 2015-04-10 | 2016-12-01 | チャンネル コマーシャル コーポレイション | Thermosetting polymer public equipment storage room cover |
Families Citing this family (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP5142002B2 (en) * | 2004-05-11 | 2013-02-13 | 日東紡績株式会社 | Transparent incombustible sheet and method for producing the same |
JP5142055B2 (en) * | 2010-11-24 | 2013-02-13 | 日東紡績株式会社 | Smoke barrier wall made of transparent incombustible sheet |
-
1989
- 1989-05-12 JP JP1117441A patent/JPH02297425A/en active Granted
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH04249542A (en) * | 1990-12-19 | 1992-09-04 | Matsushita Electric Works Ltd | Production of thin smc sheet |
JP2016199996A (en) * | 2015-04-10 | 2016-12-01 | チャンネル コマーシャル コーポレイション | Thermosetting polymer public equipment storage room cover |
US10358285B2 (en) | 2015-04-10 | 2019-07-23 | Channell Commercial Corporation | Thermoset polymer utility vault lid |
Also Published As
Publication number | Publication date |
---|---|
JPH0567415B2 (en) | 1993-09-24 |
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