JPH026954B2 - - Google Patents
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- Publication number
- JPH026954B2 JPH026954B2 JP57154664A JP15466482A JPH026954B2 JP H026954 B2 JPH026954 B2 JP H026954B2 JP 57154664 A JP57154664 A JP 57154664A JP 15466482 A JP15466482 A JP 15466482A JP H026954 B2 JPH026954 B2 JP H026954B2
- Authority
- JP
- Japan
- Prior art keywords
- pipe
- pps
- resin
- frp
- fiber
- 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 - Lifetime
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- Protection Of Pipes Against Damage, Friction, And Corrosion (AREA)
- Rigid Pipes And Flexible Pipes (AREA)
- Laminated Bodies (AREA)
Description
本発明は、ポリフエニレンサルフアイド(以下
PPSと略記する)製パイプを芯材とし、その外層
として円周方向に繊維強化熱硬化性樹脂(以下、
FRPと略記する)にて被覆した耐食性、耐薬品
性、耐熱性、強度、剛性等に優れる複合樹脂パイ
プに関するものである。
従来、PPSはポリ四フツ化エチレン(テフロ
ン)樹脂に匹敵する優れた耐食性、耐薬品性およ
び優れた耐熱性を生かして、射出成形法による各
種自動車部品、電子電気機器部品への応用、粉末
PPSを用い金属へのコーテイングなどの分野に使
用されている。このPPSを化学プラントなどの配
管用として、押出成形法によりパイプを製作した
場合、強度、剛性が低く、パイプ内を通過する流
体の圧力に耐えられず、破壊するという欠点を有
している。これを防止するために、PPSをガラス
繊維、カーボン繊維などで強化することが考えら
れるが、ガラス繊維、カーボン繊維などを含むコ
ンパウンドを用いて押出成形によりパイプを成形
する工程で、繊維がパイプの軸方向に配向するの
で、パイプの円周方向には、ほとんど強化効果が
無く、内圧に耐えることができない欠点がある。
一方、FRPパイプは、ガラス繊維、カーボン繊
維、その他のロービングに樹脂を含浸させなが
ら、マンドレルに巻きつけたり、ダイスで引抜い
たりして管状に成形することにより製造される。
しかしながら、FRPに使用される樹脂は、不飽
和ポリエステル、エポキシ樹脂などに代表される
熱硬化性樹脂が主なものであり、これらで成形さ
れる管は鋼管よりは耐食性に優れるものの、PPS
樹脂の耐食性、耐溶剤性、耐熱性には全く及ばな
い。更に、管成形時にマンドレルを使用するた
め、マンドレルの脱着工程などが必要となるなど
の工程上効率が悪い。
本発明者は、PPSが他の熱可塑性樹脂に比べ
て、特に耐薬品性、耐溶剤性、耐熱性、長期寸法
安定性に優れており、瞬間的には260℃、長期間
では220〜240℃の高温で使用に耐え、その上この
様な高温雰囲気中でも、ほとんどあらゆる薬品、
溶剤に侵されないという特長を持つており、この
ような特性を持つたプラスチツクス材料がPPS以
外にほとんど見られない点に着目し、上記欠点を
改良するために鋭意研究の結果、夫々の単体素材
の特長を生かし、欠点を克服したユニークな樹脂
複合パイプを完成するに至つた。
即ち、本発明はPPS製パイプを芯材とし、その
表面に繊維強化熱硬化性樹脂で被覆してなる耐食
性、耐薬品性、耐熱性、強度、剛性等に優れる複
合樹脂パイプを提供するものである。
本発明の複合樹脂パイプは、通常フイラメント
ワインデイング装置により押出成形されたPPSパ
イプの外表面にFRPワインデイング層を被覆す
ることによつて一体構造となり、耐食性、耐薬品
性、耐熱性、強度、剛性にすぐれたものとなる。
本発明の特長は、耐薬品性、耐熱性に極めて優
れたPPSパイプを芯材にすることにより、補強層
であるFRP層の耐薬品性、特に耐溶剤性の低さ
を補つた点にある。更に、FRPパイプと比較し
て製造に際してマンドレルを使用しなくとも、
PPSパイプがその役目を兼ねるという付加的な効
果がある。
本発明の複合樹脂パイプの製造は、例えば押出
成形で得られたPPSパイプを芯材にして熱硬化性
樹脂で含浸された補強材、例えば5〜20ミクロン
径のガラス繊維を数百本集束したガラスロービン
グなどをフイラメントワインデイング装置で、好
ましくは芯材の円周方向に所望のワインデイング
角度で巻きつけた後、加熱あるいは光、紫外線、
遠赤外線等の照射によつて硬化せしめることによ
つて得られる。
本発明に使用するPPSは一般式
The present invention is based on polyphenylene sulfide (hereinafter referred to as polyphenylene sulfide).
The core material is a pipe made of fiber-reinforced thermosetting resin (abbreviated as PPS), and the outer layer is a fiber-reinforced thermosetting resin (hereinafter referred to as
This relates to composite resin pipes coated with FRP (abbreviated as FRP) that have excellent corrosion resistance, chemical resistance, heat resistance, strength, rigidity, etc. Conventionally, PPS has been applied to various automobile parts and electronic and electrical equipment parts by injection molding, and has been used as a powder by taking advantage of its excellent corrosion resistance, chemical resistance, and heat resistance comparable to polytetrafluoroethylene (Teflon) resin.
PPS is used in fields such as coating metals. When pipes are manufactured using extrusion molding using PPS for piping in chemical plants, etc., they have the disadvantage of low strength and rigidity, and cannot withstand the pressure of the fluid passing through the pipes, causing them to break. To prevent this, it is possible to strengthen PPS with glass fiber, carbon fiber, etc., but in the process of forming pipes by extrusion molding using compounds containing glass fibers, carbon fibers, etc. Since it is oriented in the axial direction, it has almost no reinforcing effect in the circumferential direction of the pipe and has the disadvantage of not being able to withstand internal pressure.
On the other hand, FRP pipes are manufactured by impregnating glass fibers, carbon fibers, or other rovings with resin and forming them into a tubular shape by winding them around a mandrel or drawing them with a die.
However, the resins used in FRP are mainly thermosetting resins such as unsaturated polyester and epoxy resins, and although pipes made of these resins have better corrosion resistance than steel pipes, PPS
It does not match the corrosion resistance, solvent resistance, and heat resistance of resin at all. Furthermore, since a mandrel is used during tube forming, a process of attaching and detaching the mandrel is required, resulting in poor process efficiency. The present inventor found that PPS has particularly excellent chemical resistance, solvent resistance, heat resistance, and long-term dimensional stability compared to other thermoplastic resins, and has a temperature of 260°C momentarily and 220-240°C over a long period of time. It can withstand use at high temperatures of ℃, and even in such a high temperature atmosphere, it can withstand almost all kinds of chemicals.
It has the characteristic of not being attacked by solvents, and we focused on the fact that there are almost no plastic materials other than PPS that have this characteristic, and as a result of intensive research to improve the above disadvantages, we developed each individual material. We have completed a unique resin composite pipe that takes advantage of the features and overcomes the drawbacks. That is, the present invention provides a composite resin pipe having excellent corrosion resistance, chemical resistance, heat resistance, strength, rigidity, etc., which is made of a PPS pipe as a core material and whose surface is coated with a fiber-reinforced thermosetting resin. be. The composite resin pipe of the present invention has an integral structure by coating the outer surface of a PPS pipe extruded with a filament winding device with an FRP winding layer, and has excellent corrosion resistance, chemical resistance, heat resistance, strength, It has excellent rigidity. The feature of the present invention is that by using PPS pipe as the core material, which has extremely excellent chemical resistance and heat resistance, it compensates for the low chemical resistance, especially solvent resistance, of the FRP layer, which is the reinforcing layer. . Furthermore, compared to FRP pipes, there is no need to use a mandrel during manufacturing.
There is an additional effect that the PPS pipe also serves this purpose. The composite resin pipe of the present invention is manufactured by using, for example, a PPS pipe obtained by extrusion molding as a core material and a reinforcing material impregnated with a thermosetting resin, such as several hundred glass fibers with a diameter of 5 to 20 microns, bundled together. After winding glass roving or the like with a filament winding device, preferably in the circumferential direction of the core material at a desired winding angle, it is heated, exposed to light, ultraviolet rays, etc.
It is obtained by curing by irradiation with far infrared rays or the like. The PPS used in the present invention has the general formula
【式】で示される構成単位を90モル%
以上含むものが好ましく、その量が90モル%未満
のものは物性が劣る。このポリマーの重合法とし
ては、p−ジクロルベンゼンを硫黄と炭酸ソーダ
の存在下で重合させる方法、極性溶媒中で硫化ナ
トリウムあるいは水硫化ナトリウムと水酸化ナト
リウム又は硫化水素と水酸化ナトリウムの存在下
で重合させる方法、p−クロルチオフエノールの
自己縮合などがあげられるが、N−メチルピロリ
ドン、ジメチルアセトアミドなどのアミド系溶媒
やスルホラン等のスルホン系溶媒中で硫化ナトリ
ウムとp−ジクロルベンゼンを反応させる方法が
適当である。この際に重合度を調節するためにカ
ルボン酸やスルホン酸のアルカリ金属塩を添加し
たり、水酸化アルカリを添加することは好ましい
方法である。共重合成分として10モル%未満であ
ればメタ結合(Those containing 90 mol% or more of the structural unit represented by the formula are preferable, and those containing less than 90 mol% have poor physical properties. Polymerization methods for this polymer include a method in which p-dichlorobenzene is polymerized in the presence of sulfur and sodium carbonate, a method in which p-dichlorobenzene is polymerized in the presence of sulfur and sodium carbonate, and a method in which p-dichlorobenzene is polymerized in the presence of sodium sulfide, sodium bisulfide and sodium hydroxide, or hydrogen sulfide and sodium hydroxide in a polar solvent. Examples include polymerization with p-chlorothiophenol, self-condensation of p-chlorothiophenol, etc., but the reaction of sodium sulfide with p-dichlorobenzene in an amide solvent such as N-methylpyrrolidone or dimethylacetamide, or a sulfonic solvent such as sulfolane may be used. An appropriate method is to At this time, in order to adjust the degree of polymerization, it is a preferable method to add an alkali metal salt of carboxylic acid or sulfonic acid, or to add alkali hydroxide. If it is less than 10 mol% as a copolymer component, a meta bond (
【式】)、エーテル結 合([Formula]), ether bond If (
【式】)、スルホン結 合([Formula]), sulfone bond If (
【式】)、ビフエニ ル結合([Formula]), bihueni le join (
【式】)、置換フ エニルスルフイド結合([expression]), replacement enyl sulfide bond (
【式】ここ
でRはアルキル、ニトロ、フエニル、アルコキシ
基を示す)、3官能フエニルスルフイド結合
([Formula] Here, R represents an alkyl, nitro, phenyl, or alkoxy group), a trifunctional phenyl sulfide bond (
【式】)などを含有していてもポリ
マーの結晶性に大きく影響しない範囲でかまわな
いが好ましくは共重合成分は5モル%以下がよ
い。特に3官能性以上のフエニル、ビフエニル、
ナフチルスルフイド結合などを共重合に選ぶ場合
は3モル%以下、さらに好ましくは1モル%以下
がよい。
かかるPPSは一般的な製造法、例えば(1)ハロゲ
ン置換芳香族化合物と硫化アルカリとの反応(米
国特許第2513188号明細書、特公昭44−27671号お
よび特公昭45−3368号参照)(2)チオフエノール類
のアルカリ触媒又は銅塩等の共存下における縮合
反応(米国特許第3274165号、英国特許第1160660
号参照)(3)芳香族化合物を塩化硫黄とのルイス酸
触媒共存下に於ける縮合反応(特公昭46−27255
号、ベルギー特許第29437号参照)等により合成
されるものであり、目的に応じ任意に選択し得
る。
更にPPSの50重量%以下の割合で、テフロン樹
脂、ポリアミド、ポリカーボネート、ポリサルホ
ン、ポリアリルサルホン、ポリエーテルサルホ
ン、ポリイミド、ポリアミドイミド、エポキシ樹
脂、ポリエチレン、ポリプロピレン、PET、
PBT等の各種樹脂を添加できる。又、PPS中に
ガラス繊維、炭素繊維、金属繊維、チタン酸カリ
ウム、アスベスト、炭化ケイ素、セラミツク繊
維、窒化ケイ素などの繊維状強化剤;硫酸バリウ
ム、硫酸カルシウム、カオリン、クレー、パイロ
フイライト、ベントナイト、セリサイト、ゼオラ
イト、マイカ、雲母、ネフエリンシナイト、タル
ク、アタルパルジヤイト、ウオラストナイト、プ
ロセスドミネラルフアイバー(PMF)、フエライ
ト、硅酸カルシウム、炭酸カルシウム、炭酸マグ
ネシウム、ドロマイト、三酸化アンモン、酸化亜
鉛、酸化チタン、酸化マグネシウム、酸化鉄、二
硫化モリブデン、黒鉛、石コウ、ガラスビーズ、
ガラスバルーン、石英粉などの無機充填材を組成
物中0.1〜70重量%まで含有せしめることができ
る。これらの強化剤又は充填材を加える場合、公
知シランカツプリング剤やチタネートカツプリン
グ剤を用いることができる。
次にFRPに使用する熱硬化性樹脂としては、
不飽和ポリエステル樹脂、不飽和モノカルボン酸
変性ビニルエステル樹脂、エポキシ樹脂等が有用
である。又、補強材としてはガラス繊維、カーボ
ン繊維、ケプラ繊維、ナイロン、ポリエステル、
レーヨン、金属等のロービングが有用であり、そ
れらの織物も使用できるが、特にガラスロービン
グが好ましい。
本発明のパイプを構成するFRP層は、一定の
交叉角を有するフイラメントワインデイング層の
他にパイプ軸方向に配列したFRPの引抜き層が
存在しても良い。又、FRPの外層に、耐薬品性、
滑性を高めるために、種々の熱可塑性樹脂、例え
ば、PPS樹脂、ポリエチレン、ポリプロピレン、
PBT、ポリブデン樹脂、ポリスチレン系(例え
ばAS、ABSなど)、ポリアミド系、ポリ塩化ビ
ニル系、フツ素樹脂(例えばポリフツ化ビニル、
ポリ三フツ化エチレン)、ポリウレタンなどをは
じめとする各種熱可塑性樹脂を押出機、フローコ
ーター等で溶融して被覆するか、溶剤に溶かして
被覆するか、粉体にして被覆することができる。
次に、本発明の複合パイプを実施例にもとづい
て説明する。
実施例
線状高分子量PPS(ASTMD 1238に従つて、
315.5℃、5000g荷重で、メルトフローを測定し、
50g/10分の粘度を有するPPS)を内径25mm、外
径28mmのパイプに毎分1〜2mの速度で、押出機
バレル温度290℃にて押出成形して内径25mm、外
径28mmのパイプを連続的に得、サイジングしなが
ら水冷の後、その外表面を100番のサンドペーパ
ーで粗面に仕上げた。この押出パイプを芯材1と
し、次に、ガラスロービングに硬化剤としてメチ
ルエチルケトンパーオキサイドを1.0重量部、促
進剤として6%ナフテン酸コバルト0.1重量部を
配合したポリライト
NS−260(大日本インキ化
学工業(株)製不飽和ポリエステル樹脂)を含浸させ
たものを、芯材1の外周面にパイプの軸方向に対
し±52゜のらせん角で巻きつけ、遠赤外線加熱に
より80〜120℃に昇温させた気流中を2〜10分間
通過させることにより、FRP層を完全に硬化さ
せた。出来上つた複合パイプは第1図に示す如く
の断面形状を有し、外径32mmで、FRP中のガラ
ス体積含有率は50%であつた。このパイプは内庄
破壊テストに於て、同一の内径、外径のPPS押出
パイプと比較して、約4倍の強度を有していた。
又、複合パイプに80℃の熱濃硫酸を1.5気圧で20
時間通したが、何ら変化が認められなかつた。
又、そのパイプを切断して観察したが、PPS層の
異常は認められなかつた。
比較例
エポキシ樹脂(シエル化学社製、エピコート
828)100重量部、硬化剤として液状の酸無水物
(大日本インキ化学社製、エピクロンP−570)85
重量部、および硬化促進剤としてジメチルベンジ
ルアミン1重量部を混合し、ガラスロービングを
含浸させたものを、外径25mmのマンドレルに、ら
せん角±52゜で巻きつけた後、150℃/30分オーブ
ンで硬化させ、外径φ28内径φ25のエポキシ−GF
フイラメントワインデイングパイプを得た。
更に、上記パイプを芯材として実施例と同じ方
法で、ポリエステル−GFを外層とする二重パイ
プを得た。
このパイプに80℃の熱濃硫酸を、1.5気圧で通
した所、約5時間後に負荷圧が無くなり、パイプ
の外面より硫酸が漏れるのが確認された。パイプ
を切断し、内面観察の結果、エポキシパイプ層が
白化、膨潤し、劣化しているのが観察された。[Formula]) may be contained as long as it does not significantly affect the crystallinity of the polymer, but preferably the copolymerization component is 5 mol % or less. Especially trifunctional or higher functional phenyl, biphenyl,
When a naphthyl sulfide bond or the like is selected for copolymerization, the amount is preferably 3 mol% or less, more preferably 1 mol% or less. Such PPS can be produced by common manufacturing methods, such as (1) reaction of a halogen-substituted aromatic compound with an alkali sulfide (see U.S. Pat. No. 2,513,188, Japanese Patent Publication No. 44-27671 and Japanese Patent Publication No. 45-3368) (2) ) Condensation reaction of thiophenols in the presence of an alkali catalyst or copper salt (US Patent No. 3274165, British Patent No. 1160660)
(3) Condensation reaction of aromatic compounds with sulfur chloride in the coexistence of a Lewis acid catalyst (Special Publication No. 46-27255)
(see Belgian Patent No. 29437), and can be arbitrarily selected depending on the purpose. Furthermore, in a proportion of 50% by weight or less of PPS, Teflon resin, polyamide, polycarbonate, polysulfone, polyallylsulfone, polyethersulfone, polyimide, polyamideimide, epoxy resin, polyethylene, polypropylene, PET,
Various resins such as PBT can be added. In addition, fibrous reinforcing agents such as glass fiber, carbon fiber, metal fiber, potassium titanate, asbestos, silicon carbide, ceramic fiber, and silicon nitride are added to PPS; barium sulfate, calcium sulfate, kaolin, clay, pyrofluorite, and bentonite. , sericite, zeolite, mica, mica, nephelinsinite, talc, attalpalgite, wollastonite, processed mineral fiber (PMF), ferrite, calcium silicate, calcium carbonate, magnesium carbonate, dolomite, trioxide Ammonium, zinc oxide, titanium oxide, magnesium oxide, iron oxide, molybdenum disulfide, graphite, gypsum, glass beads,
Inorganic fillers such as glass balloons and quartz powder can be contained in the composition in an amount of 0.1 to 70% by weight. When adding these reinforcing agents or fillers, known silane coupling agents or titanate coupling agents can be used. Next, the thermosetting resin used for FRP is:
Unsaturated polyester resins, unsaturated monocarboxylic acid-modified vinyl ester resins, epoxy resins, and the like are useful. In addition, reinforcing materials include glass fiber, carbon fiber, Kepra fiber, nylon, polyester,
Rovings of rayon, metal, etc. are useful, and woven fabrics thereof can also be used, but glass rovings are particularly preferred. In the FRP layer constituting the pipe of the present invention, in addition to the filament winding layer having a constant intersecting angle, there may be a drawn layer of FRP arranged in the axial direction of the pipe. In addition, the outer layer of FRP has chemical resistance,
To improve lubricity, various thermoplastic resins such as PPS resin, polyethylene, polypropylene,
PBT, polybutene resin, polystyrene type (e.g. AS, ABS, etc.), polyamide type, polyvinyl chloride type, fluororesin (e.g. polyvinyl fluoride,
Various thermoplastic resins such as poly(ethylene trifluoride), polyurethane, etc. can be melted and coated using an extruder, flow coater, etc., coated by dissolving them in a solvent, or coated in powder form. Next, the composite pipe of the present invention will be explained based on examples. Examples Linear high molecular weight PPS (according to ASTMD 1238)
Melt flow was measured at 315.5℃ and 5000g load.
A pipe with an inner diameter of 25 mm and an outer diameter of 28 mm is extruded at a speed of 1 to 2 m/min at an extruder barrel temperature of 290°C. After being continuously obtained and water-cooled while sizing, the outer surface was roughened with 100-grit sandpaper. This extruded pipe was used as the core material 1, and then Polylite NS-260 (Dainippon Ink & Chemicals Co., Ltd. Co., Ltd.'s unsaturated polyester resin) is wrapped around the outer circumferential surface of the core material 1 at a helical angle of ±52° with respect to the axial direction of the pipe, and the temperature is raised to 80 to 120°C by far infrared heating. The FRP layer was completely cured by passing through the air stream for 2 to 10 minutes. The resulting composite pipe had a cross-sectional shape as shown in Figure 1, an outer diameter of 32 mm, and a glass volume content of 50% in FRP. This pipe had approximately 4 times the strength in an internal fracture test compared to an extruded PPS pipe with the same inner and outer diameters.
In addition, hot concentrated sulfuric acid at 80℃ was added to the composite pipe at 1.5 atm for 20 minutes.
I passed the test for a while, but no change was observed.
In addition, the pipe was cut and observed, but no abnormality was found in the PPS layer. Comparative example Epoxy resin (manufactured by Ciel Chemical Co., Ltd., Epicoat
828) 100 parts by weight, liquid acid anhydride as curing agent (manufactured by Dainippon Ink Chemical Co., Ltd., Epicron P-570) 85
parts by weight and 1 part by weight of dimethylbenzylamine as a curing accelerator, impregnated with glass roving, and wound around a mandrel with an outer diameter of 25 mm at a helical angle of ±52°, and then heated at 150°C for 30 minutes. Epoxy-GF cured in oven with outer diameter φ28 and inner diameter φ25
Obtained a filament winding pipe. Furthermore, a double pipe with polyester-GF as the outer layer was obtained in the same manner as in the example using the above pipe as the core material. When heated concentrated sulfuric acid at 80°C was passed through this pipe at 1.5 atm, the load pressure disappeared after about 5 hours, and sulfuric acid was confirmed to leak from the outside of the pipe. When the pipe was cut and the inner surface was observed, it was observed that the epoxy pipe layer had whitened, swelled, and deteriorated.
第1図は実施例で得られた複合パイプの部分剥
離斜視図であり、1はPPS芯材、2はFRPフイ
ラメントワインデイング層である。
FIG. 1 is a partially peeled perspective view of a composite pipe obtained in an example, in which 1 is a PPS core material and 2 is an FRP filament winding layer.
Claims (1)
とし、その表面に、繊維強化熱硬化性樹脂で被覆
してなる耐食性、耐薬品性、耐熱性、強度、剛性
等に優れる複合樹脂パイプ。1. A composite resin pipe with excellent corrosion resistance, chemical resistance, heat resistance, strength, rigidity, etc., which is made by using a polyphenylene sulfide pipe as a core material and coating the surface with fiber-reinforced thermosetting resin.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP15466482A JPS5947590A (en) | 1982-09-07 | 1982-09-07 | Composite-resin pipe |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP15466482A JPS5947590A (en) | 1982-09-07 | 1982-09-07 | Composite-resin pipe |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS5947590A JPS5947590A (en) | 1984-03-17 |
| JPH026954B2 true JPH026954B2 (en) | 1990-02-14 |
Family
ID=15589186
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP15466482A Granted JPS5947590A (en) | 1982-09-07 | 1982-09-07 | Composite-resin pipe |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS5947590A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US7861603B2 (en) | 2008-01-07 | 2011-01-04 | Keyence Corporation | Coriolis mass flowmeter including an inner pipe made of fluororesin and outer pipe having fibers |
Families Citing this family (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2590250B2 (en) * | 1989-01-30 | 1997-03-12 | 東レ株式会社 | Plastic tubular body |
| JPH0735180Y2 (en) * | 1989-06-05 | 1995-08-09 | 関西テック株式会社 | Pipe for ozone piping |
| JP3027386B2 (en) * | 1990-03-05 | 2000-04-04 | 呉羽化学工業株式会社 | Polyarylene thioether resin composition and extruded product |
| CA2141993C (en) * | 1994-02-07 | 2005-06-07 | Takashi Tsuda | Tubular extrusion molding product comprising high molecular weight polyarylene sulfide |
| CN102518879B (en) * | 2011-12-30 | 2013-08-14 | 上海长园电子材料有限公司 | Double-layered composite pipe, manufacturing method thereof and manufacturing equipment |
| KR101935311B1 (en) * | 2016-02-23 | 2019-04-08 | 주식회사 동일씨앤이 | Dual composite material duct |
Family Cites Families (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS4873812A (en) * | 1971-12-30 | 1973-10-05 | ||
| JPS5620969A (en) * | 1979-07-27 | 1981-02-27 | Hitachi Ltd | Absorption refrigerating machine |
-
1982
- 1982-09-07 JP JP15466482A patent/JPS5947590A/en active Granted
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US7861603B2 (en) | 2008-01-07 | 2011-01-04 | Keyence Corporation | Coriolis mass flowmeter including an inner pipe made of fluororesin and outer pipe having fibers |
Also Published As
| Publication number | Publication date |
|---|---|
| JPS5947590A (en) | 1984-03-17 |
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