JPH04191029A - Resin fuel tank - Google Patents
Resin fuel tankInfo
- Publication number
- JPH04191029A JPH04191029A JP32124090A JP32124090A JPH04191029A JP H04191029 A JPH04191029 A JP H04191029A JP 32124090 A JP32124090 A JP 32124090A JP 32124090 A JP32124090 A JP 32124090A JP H04191029 A JPH04191029 A JP H04191029A
- Authority
- JP
- Japan
- Prior art keywords
- matrix phase
- fuel tank
- continuous matrix
- resin
- gasoline
- 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.)
- Pending
Links
- 239000011347 resin Substances 0.000 title claims abstract description 25
- 229920005989 resin Polymers 0.000 title claims abstract description 25
- 239000002828 fuel tank Substances 0.000 title claims abstract description 23
- 239000011159 matrix material Substances 0.000 claims abstract description 21
- 229920000098 polyolefin Polymers 0.000 claims abstract description 7
- 239000010419 fine particle Substances 0.000 claims description 13
- 229920006122 polyamide resin Polymers 0.000 claims description 6
- 239000000463 material Substances 0.000 claims description 3
- 239000003502 gasoline Substances 0.000 abstract description 14
- 238000000034 method Methods 0.000 abstract description 14
- 239000002245 particle Substances 0.000 abstract description 12
- 238000004519 manufacturing process Methods 0.000 abstract description 7
- 239000010445 mica Substances 0.000 abstract description 6
- 229910052618 mica group Inorganic materials 0.000 abstract description 6
- 239000000446 fuel Substances 0.000 abstract description 4
- 229920002647 polyamide Polymers 0.000 abstract description 3
- 239000000454 talc Substances 0.000 abstract description 3
- 229910052623 talc Inorganic materials 0.000 abstract description 3
- 239000010954 inorganic particle Substances 0.000 abstract 1
- 239000010410 layer Substances 0.000 description 21
- 239000004677 Nylon Substances 0.000 description 13
- 229920001778 nylon Polymers 0.000 description 13
- 230000000694 effects Effects 0.000 description 8
- 229920001903 high density polyethylene Polymers 0.000 description 8
- 239000004700 high-density polyethylene Substances 0.000 description 8
- 238000000071 blow moulding Methods 0.000 description 5
- 239000006185 dispersion Substances 0.000 description 5
- -1 polyethylene Polymers 0.000 description 4
- 239000000853 adhesive Substances 0.000 description 3
- 230000001070 adhesive effect Effects 0.000 description 3
- 230000006866 deterioration Effects 0.000 description 3
- 238000002156 mixing Methods 0.000 description 2
- 230000002265 prevention Effects 0.000 description 2
- PXGOKWXKJXAPGV-UHFFFAOYSA-N Fluorine Chemical compound FF PXGOKWXKJXAPGV-UHFFFAOYSA-N 0.000 description 1
- 239000004705 High-molecular-weight polyethylene Substances 0.000 description 1
- 239000004952 Polyamide Substances 0.000 description 1
- 239000004698 Polyethylene Substances 0.000 description 1
- 239000004743 Polypropylene Substances 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 238000007664 blowing Methods 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 229920001577 copolymer Polymers 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 229910052731 fluorine Inorganic materials 0.000 description 1
- 239000011737 fluorine Substances 0.000 description 1
- 238000002844 melting Methods 0.000 description 1
- 230000008018 melting Effects 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 238000000465 moulding Methods 0.000 description 1
- 238000006386 neutralization reaction Methods 0.000 description 1
- 230000035515 penetration Effects 0.000 description 1
- 230000035699 permeability Effects 0.000 description 1
- 229920001748 polybutylene Polymers 0.000 description 1
- 229920000573 polyethylene Polymers 0.000 description 1
- 229920001155 polypropylene Polymers 0.000 description 1
- 239000002356 single layer Substances 0.000 description 1
Landscapes
- Blow-Moulding Or Thermoforming Of Plastics Or The Like (AREA)
Abstract
Description
【発明の詳細な説明】
〈産業上の利用分野〉
本発明は、樹脂製の燃料タンクに関し、ガソリン等の燃
料の透過を完全に防止するように工夫したものである。DETAILED DESCRIPTION OF THE INVENTION <Industrial Application Field> The present invention relates to a resin fuel tank, which is devised to completely prevent permeation of fuel such as gasoline.
〈従来の技術〉
燃料タンクはほとんどが金属製であるが、軽量であると
共に容易に自由な形状に成形できる点を考慮して、樹脂
製の燃料タンクが検討されている。しかし、一般の樹脂
は、ガソリン等が完全に遮断することができず、多少の
透過性を有するので、成形した後に処理等を施してガソ
リン等の透過を完全に防止する必要がある。そこで、下
記のような樹脂製燃料タンクが提案されている。<Prior Art> Most fuel tanks are made of metal, but fuel tanks made of resin are being considered because they are lightweight and can be easily molded into any shape. However, general resins cannot completely block out gasoline and the like and have some permeability, so it is necessary to perform treatment after molding to completely prevent the penetration of gasoline and the like. Therefore, the following resin fuel tank has been proposed.
第一には、例えば高密度ポリエチレン
(HDPE)を単層にブロー成形した後、その成形品中
にSOガスを入れてオートクレーブ中で処理し、続いて
NH,ガスで中和することにより、成形品内面をS03
処理する方法である。First, for example, high-density polyethylene (HDPE) is blow-molded into a single layer, and then SO gas is introduced into the molded product and treated in an autoclave, followed by neutralization with NH gas. The inside of the product is S03
It is a method of processing.
第二には、HDPEをブロー成形する際にその内部に例
えば1%のF2ガスを吹き込み、成形品内面をフッ素処
理する方法である。The second method is to blow 1% F2 gas into the HDPE during blow molding to treat the inner surface of the molded product with fluorine.
また、第三には、ガソリンを完全に透過しないナイロン
層を中央にしてその両側にHDPE層を形成するように
ブロー成形する方法である。この場合、中央のナイロン
層とその両側のHDPE層との間に接着剤が入るので三
種五層のブロー成形品となる。The third method is to blow mold a nylon layer that is completely impermeable to gasoline so that HDPE layers are formed on both sides of the center nylon layer. In this case, the adhesive is inserted between the central nylon layer and the HDPE layers on both sides, resulting in a blow-molded product with three types and five layers.
しかし、これらの方法は、何れも製造工程や製造装置が
複雑となって製造コストが嵩むという問題がある。そこ
で、製造工程が単純な、いわゆるナイロン分散法という
方法が注目されている。この方法はHDPEにポリアミ
ド系I/M脂、例えばナイロンに接着剤を加えたシーク
(商品名;デュポン社製)を混合して重層ブロー成形す
る方法である。かがる方法によると、第2図に示すよう
にHDPEの連続マトリックス相1の厚さ方向中央部に
ポリアミド系樹脂からなる複数のラミナ層2が形成され
る。このラミナ層2は不連続であるが上記厚さ方向に直
交する方向に延びるものであり、ガソリンの透過を防止
する作用を有する。However, all of these methods have a problem in that the manufacturing process and manufacturing equipment become complicated and the manufacturing cost increases. Therefore, a method called the so-called nylon dispersion method, which has a simple manufacturing process, is attracting attention. This method is a method in which HDPE is mixed with polyamide-based I/M resin, such as SEEK (trade name; manufactured by DuPont), which is nylon with an adhesive added, and multilayer blow molding is performed. According to the darning method, as shown in FIG. 2, a plurality of lamina layers 2 made of polyamide resin are formed at the center in the thickness direction of the continuous matrix phase 1 of HDPE. This lamina layer 2 is discontinuous but extends in a direction perpendicular to the thickness direction, and has the function of preventing gasoline from permeating.
〈発明が解決しようとする課題〉
前述したナイロン分散法で、連続マトリックス相1の中
にナイロンのラミナ層2が形成されるのは1.融点が異
なるHDPEとナイロンとが相溶せずに適度に混す合っ
た状態で延伸されるからである。しかし、ラミナ層2が
形成される温度条件等の範囲が狭く、常にラミナ層2が
適正に形成されているかどうか判らないという問題があ
る。すなわち、条件によってはナイロンが粒状となり、
透過防止効果が発現しない。また、ラミナ層2が適正に
形成しても前述した多層構造のものと比べると、透過防
止効果が約1/10程度と低いという問題がある。<Problems to be Solved by the Invention> In the above-mentioned nylon dispersion method, the formation of the nylon lamina layer 2 in the continuous matrix phase 1 is as follows: 1. This is because HDPE and nylon, which have different melting points, are not miscible and are stretched in a properly mixed state. However, there is a problem that the range of temperature conditions etc. under which the lamina layer 2 is formed is narrow, and it is not always clear whether the lamina layer 2 is formed properly. In other words, depending on the conditions, nylon becomes granular,
The permeation prevention effect does not appear. Further, even if the lamina layer 2 is formed properly, there is a problem that the permeation prevention effect is about 1/10 as low as that of the multilayer structure described above.
本発明はこのような事情に鑑み、製造が容易であり、且
つガソリン等の燃料の透過の心配のない樹脂製燃料タン
クを提供することを目的とする。In view of these circumstances, an object of the present invention is to provide a resin fuel tank that is easy to manufacture and free from the risk of permeation of fuel such as gasoline.
〈I!題を解決するための手段〉
前記目的を達成する本発明に係る樹脂製燃料タンクは、
ポリオレフィンからなる連続マトリックス相の厚さ方向
中央部にポリアミド系樹脂からなると共に上記厚さ方向
に略直交する方向に延びる不連続の被数のラミナ層を有
する樹脂成形材からなる燃料タンクであって、上記連続
マトリックス相にはその面方向と略平行に偏平微粒子が
分散されていることを特徴とする。<I! Means for Solving the Problem> A resin fuel tank according to the present invention that achieves the above object has the following features:
A fuel tank made of a resin molded material having a continuous matrix phase made of polyolefin and a discontinuous number of lamina layers made of a polyamide resin and extending in a direction substantially perpendicular to the thickness direction in the central part in the thickness direction of the continuous matrix phase made of polyolefin, , the continuous matrix phase is characterized in that flat fine particles are dispersed substantially parallel to the plane direction of the continuous matrix phase.
く作 用〉
前記構成においては、連続マトリックス相中の偏平微粒
子は、ラミナ層と同様に、ガソリン等が燃料タンクの壁
を透過するのを防止する。したがって、ラミナ層の作用
と相俟って、又はラミナ層の作用が完全でなくても、ガ
ソリン等の透過が完全に防止される。Effect> In the above structure, the flat fine particles in the continuous matrix phase prevent gasoline etc. from permeating through the wall of the fuel tank, similar to the lamina layer. Therefore, together with the action of the lamina layer, or even if the action of the lamina layer is not perfect, the permeation of gasoline etc. is completely prevented.
く実 施 例〉 息下、本発明を実施例に基づいて説明する。Example of implementation The present invention will now be explained based on examples.
第1図(al、(b)には本実施例の樹脂製燃料タンク
を示す。FIGS. 1A and 1B show a resin fuel tank of this embodiment.
第1図(alに示す樹脂製燃料タンク10は、第1図1
1)lに示すように、ポリオレフィンからなる連続マト
リックス相11の中に、ポリアミド系樹脂で形成された
ラミナ層12を有すると共に、偏平微粒子13が分散さ
れている。The resin fuel tank 10 shown in FIG.
1) As shown in 1, a continuous matrix phase 11 made of polyolefin has a lamina layer 12 made of a polyamide resin, and flat fine particles 13 are dispersed therein.
ここで、ラミナ層12は主に連続マトリックス相11の
厚さ方向中央部に形成され、その面方向に延びるもので
あり、これは従来のナイロン分散法で成形されたものと
同様である。Here, the lamina layer 12 is mainly formed in the central part in the thickness direction of the continuous matrix phase 11 and extends in the surface direction thereof, which is similar to that formed by the conventional nylon dispersion method.
そして、本発明では、さらに、偏平微粒子13が分散さ
れたものである。この偏平微粒子13は、連続マトリッ
クス相]1の面方向と略平行になるように分散されてお
り、ラミナ層12と同様にガソリン等の透過する作用を
有する。In the present invention, flat fine particles 13 are further dispersed. The flat fine particles 13 are dispersed so as to be substantially parallel to the surface direction of the continuous matrix phase 1, and have the function of permeating gasoline and the like like the lamina layer 12.
本発明でポリオレフィンとは、ポリエチレン、ポリプロ
ピレン、ポリブチレン等、及びこれらの二種以上の共重
合体をいう。また、ポリアミド系樹脂は、ナノロンの他
、ナイロンに接着剤を混合した樹脂をいう。In the present invention, polyolefin refers to polyethylene, polypropylene, polybutylene, etc., and copolymers of two or more of these. In addition to Nanolon, polyamide resin refers to a resin made by mixing nylon with an adhesive.
一方、偏平微粒子とは、マイカやタルクなどの無45!
−徹粒子で偏平したものをいい、その径と厚みとの比、
L/lが大きいほど好ましい。例えば粒径が20〜10
0μmで、L/lが5以上、好ましくは]0以上のもの
がよい。On the other hand, flat fine particles are free particles such as mica and talc.
- Refers to a flattened particle, the ratio of its diameter and thickness,
The larger L/l is, the more preferable. For example, the particle size is 20-10
0 μm, L/l is 5 or more, preferably ]0 or more.
粒径が20μm未満ては本発明の効果が発揮し難く、ま
た、100μmをこえろと偏平でなくなりブロック化し
易く、成形性悪化につながる。また、L / tが小さ
いと、やはりブロック化して成形性悪化につながり、本
発明の効果は得らない。このような条件を満足するもの
としては、−船釣なマイカや加工したタルク等が挙げら
れるが、マイカの場合でもさらに薄くスライスしたもの
を用いた方が大きな効果が得られる。If the particle size is less than 20 μm, it is difficult to exhibit the effects of the present invention, and if the particle size exceeds 100 μm, the particles will not be flat and will easily form into blocks, leading to deterioration of moldability. In addition, if L/t is small, it will still form into blocks, leading to deterioration of moldability, and the effects of the present invention will not be obtained. Examples of materials that satisfy these conditions include mica that has been caught on a boat and processed talc, but even in the case of mica, it is better to use thinly sliced mica to obtain a greater effect.
本実施例の樹脂製燃料タンク10は、このような偏平微
粒子13が上述したように連続マトリックス相11中に
その面方向と略平行になるように分散されているので、
たとえラミナ相12が適正に形成されていない場合でも
ガソリン等の透過が防止される。In the resin fuel tank 10 of this embodiment, such flat fine particles 13 are dispersed in the continuous matrix phase 11 so as to be substantially parallel to the surface direction thereof, as described above.
Even if the lamina phase 12 is not properly formed, permeation of gasoline etc. is prevented.
このような樹脂製燃料タンク10を製造するに(ま、ポ
リオレフィンとポリアミド系樹脂と偏平微粒子とを適度
に混合した後、従来のナイロン分散法と同様に延伸する
条件で成形すればよく、例えば、押し出した円筒体を型
に収めた後、エアーを吹き込み延伸するブロー成形によ
ればよい。このように延伸成形されることにより、偏平
微粒子は連続マトリックス相の面方向と略平行になって
分散され、ガソリン等の透過を防止する作用を果たす。In order to manufacture such a resin fuel tank 10, it is sufficient to mix polyolefin, polyamide resin, and flat fine particles appropriately, and then to form the resin under stretching conditions similar to the conventional nylon dispersion method. Blow molding may be performed in which the extruded cylindrical body is placed in a mold and then stretched by blowing air into it.By stretching in this manner, the flat fine particles are dispersed approximately parallel to the plane direction of the continuous matrix phase. , which acts to prevent the permeation of gasoline, etc.
このような偏平微粒子の配合割合は、1〜30重量%が
好ましい。1重量%未満ではその効果が発揮されず、一
方、30重量%をこえると成形性の悪化につながるから
である。The blending ratio of such flat fine particles is preferably 1 to 30% by weight. This is because if it is less than 1% by weight, the effect will not be exhibited, while if it exceeds 30% by weight, it will lead to deterioration of moldability.
ポリアミド型樹脂としてシータ (商品名:デュポン社
製)を用い、これに偏平微粒子として偏平マイカを混合
した後、これを高密度高分子量ポリエチレンに混合し、
ブロー成形により燃料タンクを作製した。かかる燃料タ
ンクは、ガソリン等の透過が完全に防止されたものであ
った。Using Theta (trade name: manufactured by DuPont) as a polyamide type resin, flattened mica was mixed with it as flattened fine particles, and then this was mixed with high-density, high-molecular-weight polyethylene.
A fuel tank was manufactured by blow molding. Such fuel tanks were completely prevented from permeating gasoline and the like.
〈発明の効果〉
以上説明したように、本発明の樹脂製燃料タンクは、ブ
ロー成形等により容易に製造でき、しかも、ラミナ層が
適正に形成されていない場合でも偏平微粒子により燃料
の透過が完全に防止されるものであり、安全性の高いも
のである。<Effects of the Invention> As explained above, the resin fuel tank of the present invention can be easily manufactured by blow molding, etc., and even if the lamina layer is not properly formed, the flat particles ensure complete fuel permeation. It is highly safe.
第1図(a)、 (blは、本発明の一実施例に係る樹
脂製燃料タンクを示す説明図、第2図は従来技術に係る
ナイロン分散法による成形体の断面図である。
図 面 中、
10は樹脂製燃料タンク、
11は連続マトリックス相、
12はラミナ層、
13は偏平微粒子である。
特 許 出 願 人
三菱自動車工業株式会社
代 理 人FIGS. 1A and 1B are explanatory diagrams showing a resin fuel tank according to an embodiment of the present invention, and FIG. 2 is a cross-sectional view of a molded body formed by a nylon dispersion method according to the prior art. Among them, 10 is a resin fuel tank, 11 is a continuous matrix phase, 12 is a lamina layer, and 13 is flat fine particles.Patent applicant: Mitsubishi Motors Corporation, agent
Claims (1)
中央部にポリアミド系樹脂からなると共に上記厚さ方向
に略直交する方向に延びる不連続の複数のラミナ層を有
する樹脂成形材からなる燃料タンクであって、上記連続
マトリックス相にはその面方向と略平行に偏平微粒子が
分散されていることを特徴とする樹脂製燃料タンク。A fuel tank made of a resin molded material having a continuous matrix phase made of polyolefin and a plurality of discontinuous lamina layers made of polyamide resin and extending in a direction substantially perpendicular to the thickness direction in the central part in the thickness direction, A resin fuel tank characterized in that the continuous matrix phase has flat fine particles dispersed substantially parallel to the surface direction of the continuous matrix phase.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP32124090A JPH04191029A (en) | 1990-11-27 | 1990-11-27 | Resin fuel tank |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP32124090A JPH04191029A (en) | 1990-11-27 | 1990-11-27 | Resin fuel tank |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH04191029A true JPH04191029A (en) | 1992-07-09 |
Family
ID=18130375
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP32124090A Pending JPH04191029A (en) | 1990-11-27 | 1990-11-27 | Resin fuel tank |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH04191029A (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2006168250A (en) * | 2004-12-17 | 2006-06-29 | Taisei Kako Co Ltd | Resin molding and its manufacturing method |
JP2010036493A (en) * | 2008-08-06 | 2010-02-18 | Yachiyo Industry Co Ltd | Multilayered plastic fuel tank |
JP2010052803A (en) * | 2008-08-29 | 2010-03-11 | Yachiyo Industry Co Ltd | Multilayer plastic fuel tank |
-
1990
- 1990-11-27 JP JP32124090A patent/JPH04191029A/en active Pending
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2006168250A (en) * | 2004-12-17 | 2006-06-29 | Taisei Kako Co Ltd | Resin molding and its manufacturing method |
JP2010036493A (en) * | 2008-08-06 | 2010-02-18 | Yachiyo Industry Co Ltd | Multilayered plastic fuel tank |
JP2010052803A (en) * | 2008-08-29 | 2010-03-11 | Yachiyo Industry Co Ltd | Multilayer plastic fuel tank |
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