JP2006095944A - Thermoplastic resin foam - Google Patents

Thermoplastic resin foam Download PDF

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JP2006095944A
JP2006095944A JP2004286602A JP2004286602A JP2006095944A JP 2006095944 A JP2006095944 A JP 2006095944A JP 2004286602 A JP2004286602 A JP 2004286602A JP 2004286602 A JP2004286602 A JP 2004286602A JP 2006095944 A JP2006095944 A JP 2006095944A
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thermoplastic resin
resin foam
sheet
inert gas
stretching
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Michiaki Kawakami
道昭 川上
Masayasu Ito
正康 伊藤
Akira Kabumoto
昭 株本
Hidefumi Miyagi
秀文 宮城
Hiroyuki Yamazaki
宏行 山崎
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Furukawa Electric Co Ltd
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Abstract

<P>PROBLEM TO BE SOLVED: To provide a thermoplastic resin foam which is suitable for a backlight and an illumination box such as an illumination fascia, a lighting equipment, a display or the like, and which has a high reflectance ratio. <P>SOLUTION: The thermoplastic resin foam is manufactured by a manufacturing method comprising: a process which makes a thermoplastic resin sheet contain inert gas by keeping it in a pressurized inert gas atmosphere; a process which heats the thermoplastic resin sheet containing inert gas and makes it to foam under an ordinary pressure; and a process which draws the foamed thermoplastic resin in at least uniaxial direction. <P>COPYRIGHT: (C)2006,JPO&NCIPI

Description

本発明は電飾看板や照明器具、ディスプレイなどのバックライトや照明ボックスに好適な熱可塑性樹脂発泡体シートに関する。 The present invention relates to a thermoplastic resin foam sheet suitable for backlights and lighting boxes such as electric signboards, lighting fixtures, and displays.

従来、電飾看板や照明器具、ディスプレイなどのバックライトに使用される光反射板として、光を反射する合成樹脂製のフィルムまたはシートを立体的な形状に加工した光反射板が提案されている(例えば特許文献1参照)。 2. Description of the Related Art Conventionally, a light reflecting plate obtained by processing a synthetic resin film or sheet that reflects light into a three-dimensional shape has been proposed as a light reflecting plate used for backlights of electric signs, lighting fixtures, and displays. (For example, refer to Patent Document 1).

光を反射する合成樹脂製のフィルムまたはシートとしては、内部に微細な気泡または気孔を多数有する熱可塑性樹脂発泡体のフィルムまたはシート(例えば特許文献2参照)や、フィラーを含有する熱可塑性樹脂のフィルムであって、フィラーを核として多数のボイドが形成されているフィルム(例えば特許文献3参照)が知られている。 As a film or sheet made of a synthetic resin that reflects light, a film or sheet of a thermoplastic resin foam having a large number of fine bubbles or pores therein (see, for example, Patent Document 2), or a thermoplastic resin containing a filler A film is known in which a large number of voids are formed using a filler as a core (see, for example, Patent Document 3).

前者の微細な気泡または気孔を多数有する熱可塑性樹脂発泡体は、溶融状態または固体状態の熱可塑性樹脂に、加圧下で不活性ガスを接触させた後、除圧し、常圧下でその樹脂の軟化温度以上に加熱して発泡させることにより得られる。得られた熱可塑性樹脂発泡体のフィルムまたはシートは、平均気泡径が50μm以下と微細であるため、高い反射率を有するとともに、優れた形状保持性を有しており、熱可塑性樹脂発泡体のフィルムまたはシート単独で立体的な形状に加工が可能である。なお、一般に熱可塑性樹脂発泡体のフィルムまたはシートの光反射率は、フィルムまたはシートの厚さが薄くなるに従い、低下する傾向にある。そこで、薄くても高い反射率を有する熱可塑性樹脂発泡体が求められている。 The former foam with a large number of fine bubbles or pores is made by bringing the molten or solid thermoplastic resin into contact with an inert gas under pressure, then depressurizing and softening the resin under normal pressure. It can be obtained by foaming by heating above the temperature. The obtained thermoplastic resin foam film or sheet has an average cell diameter as fine as 50 μm or less, and thus has high reflectivity and excellent shape retention. A film or sheet alone can be processed into a three-dimensional shape. In general, the light reflectance of a thermoplastic resin foam film or sheet tends to decrease as the thickness of the film or sheet decreases. Therefore, there is a need for a thermoplastic resin foam that is thin but has high reflectivity.

一方、後者のフィラーを含有する熱可塑性樹脂のフィルムは、炭酸カルシウムや硫酸バリウムなどのフィラーを含有する未延伸フィルムを成形し、この未延伸フィルムを延伸することにより、フィラーを核として多数のボイドを形成させることにより得られる。得られたフィルムは厚さが200μm未満と薄いため、フィルム単独では形状保持性を有さないとともに、フィルム背面へ漏洩する光も多くなる。よって、フィルムの背面に十分な強度と遮光性を有する板を配置して用いられる。 On the other hand, the film of the thermoplastic resin containing the latter filler is formed by forming an unstretched film containing a filler such as calcium carbonate or barium sulfate, and stretching the unstretched film, so that a large number of voids with the filler as a core are formed. Is obtained. Since the obtained film is as thin as less than 200 μm, the film alone does not have shape retaining property, and more light leaks to the back of the film. Therefore, a plate having sufficient strength and light shielding property is disposed on the back side of the film.

ところで、発泡ポリエステルシートを延伸して得られる結束バンドが知られている(例えば特許文献4参照)。しかし、これは発泡体を延伸することにより十分な引張強度と適度な柔軟性を有する結束用バンドが得られる旨が記載されているにすぎない。
また、溶融押出発泡体を延伸して得られる白色フィルムが知られている(例えば特許文献5および特許文献6参照)。しかしながら、特許文献5に記載されているように、溶融押出法により得られる発泡体は、気泡径が15〜400μm(実施例においては80〜350μm)と大きいため、これを延伸しても高い反射率のフィルムを得ることができない。特許文献5および6に記載されているように、ダイの圧力を維持することは、溶融押出法で微細気泡を得るために必要な条件であるが、それだけでなく出口での圧力低下率を高くとることも必要となる。これらの技術は、各種文献で公知であるが、この方法は幅が狭いフィルムでは実施可能なものの、製品レベルの広幅(たとえば600mm〜1500mm幅程度)を実施することは非常に困難である。幅が狭いフィルムを、後工程で延伸することによって広幅にすることは可能であるが、その場合は非常に薄肉のフィルムしか得られない。薄肉フィルムの場合、高反射率を得ることが難しいと共に、形状保持性や取り扱い性、組み立て加工性に劣り、特に光反射板として用いる場合には問題が生じることがある。
Incidentally, a binding band obtained by stretching a foamed polyester sheet is known (see, for example, Patent Document 4). However, this only describes that a binding band having sufficient tensile strength and appropriate flexibility can be obtained by stretching the foam.
Moreover, the white film obtained by extending | stretching a melt-extrusion foam is known (for example, refer patent document 5 and patent document 6). However, as described in Patent Document 5, since the foam obtained by the melt extrusion method has a large bubble diameter of 15 to 400 μm (80 to 350 μm in the examples), it is highly reflective even when it is stretched. Rate film can not be obtained. As described in Patent Documents 5 and 6, maintaining the pressure of the die is a necessary condition for obtaining fine bubbles by the melt extrusion method, but not only that, but also increasing the pressure drop rate at the outlet. It is also necessary to take. These techniques are known in various literatures, but although this method can be carried out with a narrow film, it is very difficult to carry out a wide product level (for example, about 600 mm to 1500 mm width). Although it is possible to widen a narrow film by stretching in a subsequent process, in that case, only a very thin film can be obtained. In the case of a thin film, it is difficult to obtain a high reflectance, and shape retention property, handling property, and assembly workability are inferior. In particular, there is a problem when used as a light reflecting plate.

特開2002−122863号公報JP 2002-122863 A WO97/01117号公報WO97 / 01117 Publication 特開平4−296819号公報Japanese Patent Laid-Open No. 4-296619 特開平10−101127号公報Japanese Patent Laid-Open No. 10-101127 特開2004−195685号公報Japanese Patent Laid-Open No. 2004-195685 特開平11−300814号公報JP-A-11-300814

近年、省電力化が求められており、より高い反射率を有する樹脂のフィルムまたはシートが要求されている。さらに、特に電飾看板やディスプレイの分野では、省スペース化のニーズが高まっており、光を反射する樹脂のフィルムまたはシートの薄型化が要求されている。しかしながら、前述のように、フィルムまたはシートを薄型化すると薄くなるに従い反射率の低下が起こり、最近の高輝度、高反射率の要求を満足する反射板が得られにくい傾向がある。また、薄型化に伴い、形状保持性の低下、折り曲げや打ち抜きなどの2次加工性が低下するという問題もある。さらに、薄いフィルムまたはシートの場合、ディスプレイのバックライトなどへ組み込む際に、位置あわせが難しく、作業効率が落ちるという問題もある。本発明は、薄型でより高い反射率を有するだけでなく、加工性や形状保持性に優れる熱可塑性樹脂発泡体を提供することを目的とする。 In recent years, power saving has been demanded, and a resin film or sheet having higher reflectivity has been demanded. Further, particularly in the field of electric signboards and displays, there is an increasing need for space saving, and a thin resin film or sheet that reflects light is required. However, as described above, when the film or sheet is made thinner, the reflectivity decreases as the film or sheet becomes thinner, and it tends to be difficult to obtain a reflector satisfying the recent requirements for high luminance and high reflectivity. In addition, as the thickness is reduced, there is a problem that the shape retainability is lowered and the secondary workability such as bending and punching is lowered. Further, in the case of a thin film or sheet, there is a problem in that it is difficult to align when incorporated in a display backlight or the like, and the work efficiency is lowered. An object of the present invention is to provide a thermoplastic resin foam that is not only thin and has a higher reflectance, but also has excellent processability and shape retention.

本発明者らは前述した課題を解決すべく鋭意検討を重ねた結果、熱可塑性樹脂シートを加圧不活性ガス雰囲気中に保持して不活性ガスを含有させる工程(以下「第1工程」という)と、不活性ガスを含有させた熱可塑性樹脂シートを常圧下で加熱して発泡させる工程(以下「第2工程」という)と、発泡した熱可塑性樹脂シートを延伸させる工程(以下「第3工程」という)とからなる製造方法により製造することにより、より高反射率を有する熱可塑性樹脂発泡体が得られることを見出した。すなわち本発明は、
(1)熱可塑性樹脂シートを加圧不活性ガス雰囲気中に保持して不活性ガスを含有させる工程と、不活性ガスを含有させた熱可塑性樹脂シートを常圧下で加熱して発泡させる工程と、発泡した熱可塑性樹脂シートを少なくとも1軸に延伸させる工程とからなる製造方法により製造された熱可塑性樹脂発泡体、
(2)前記熱可塑性樹脂発泡体の発泡倍率が2倍以上であり、かつ、前記熱可塑性樹脂発泡体のシートの厚さが250μm以上であることを特徴とする(1)に記載の熱可塑性樹脂発泡体、
(3)400〜700nmの光の波長域における平均反射率が90%以上であることを特徴とする(1)または(2)に記載の熱可塑性樹脂発泡体、
(4)前記熱可塑性樹脂がポリエステルであることを特徴とする(1)乃至(3)のいずれか1つに記載の熱可塑性樹脂発泡体、
を提供するものである。
As a result of intensive studies to solve the above-mentioned problems, the present inventors have held a thermoplastic resin sheet in a pressurized inert gas atmosphere to contain an inert gas (hereinafter referred to as “first step”). ), A step of heating and foaming a thermoplastic resin sheet containing an inert gas under normal pressure (hereinafter referred to as “second step”), and a step of stretching the foamed thermoplastic resin sheet (hereinafter referred to as “third”). It has been found that a thermoplastic resin foam having a higher reflectivity can be obtained by producing by a production method consisting of “process”. That is, the present invention
(1) A step of holding the thermoplastic resin sheet in a pressurized inert gas atmosphere to contain the inert gas, and a step of heating and foaming the thermoplastic resin sheet containing the inert gas under normal pressure, and A thermoplastic resin foam produced by a production method comprising a step of stretching a foamed thermoplastic resin sheet at least uniaxially;
(2) The thermoplastic resin according to (1), wherein the thermoplastic resin foam has an expansion ratio of 2 times or more, and a thickness of the thermoplastic resin foam sheet is 250 μm or more. Resin foam,
(3) The thermoplastic resin foam according to (1) or (2), wherein an average reflectance in a wavelength range of 400 to 700 nm is 90% or more,
(4) The thermoplastic resin foam according to any one of (1) to (3), wherein the thermoplastic resin is polyester.
Is to provide.

本発明により得られる熱可塑性樹脂発泡体は薄型化が可能であり、かつ、溶融押出発泡体を延伸して得られる熱可塑性樹脂発泡体シートに比べ、気泡径が微細であるため、従来予測し得なかった高い反射率を示す。また、本発明により得られる熱可塑性樹脂発泡体は、薄型であるにも関わらず、優れた形状保持性を有しており、熱可塑性樹脂発泡体のフィルムまたはシート単独で立体的な形状に加工が可能である。よって、ディスプレイのバックライトなどへの組み込みの作業効率が良い。更に、本発明により得られる熱可塑性樹脂発泡体は、引張伸び特性が従来の熱可塑性樹脂発泡体に比べて優れるため、立体的な形状に加工した際に、シートの割れなどの不良が発生しにくい。
すなわち、本発明により得られる熱可塑性樹脂発泡体は電飾看板や照明器具、ディスプレイなどのバックライトや照明ボックスの光反射板として好適に用いることができる。
The thermoplastic resin foam obtained by the present invention can be thinned and has a smaller cell diameter than a thermoplastic resin foam sheet obtained by stretching a melt-extruded foam. High reflectivity not obtained. In addition, the thermoplastic resin foam obtained by the present invention has excellent shape-retaining properties despite being thin, and the thermoplastic resin foam film or sheet alone is processed into a three-dimensional shape. Is possible. Therefore, the work efficiency of incorporation into the backlight of the display is good. Furthermore, since the thermoplastic resin foam obtained by the present invention has superior tensile elongation characteristics compared to conventional thermoplastic resin foams, defects such as sheet cracking occur when processed into a three-dimensional shape. Hateful.
That is, the thermoplastic resin foam obtained by the present invention can be suitably used as a backlight of an electric signboard, a lighting fixture, a display, or a light reflecting plate of an illumination box.

本発明の第1工程ではまず、熱可塑性樹脂のシートとセパレーターを重ねて巻くことによりロール形成し、このロールを加圧不活性ガス雰囲気中に保持して該熱可塑性樹脂シートに不活性ガスを含有させる。
不活性ガスとしては、ヘリウム、窒素、二酸化炭素、アルゴン、圧縮空気などが挙げられる。熱可塑性樹脂が飽和状態になるまでの不活性ガス浸透時間および不活性ガス浸透量は、発泡させる熱可塑性樹脂の種類、不活性ガスの種類、浸透圧力およびシートの厚さによって異なる。
In the first step of the present invention, first, a roll is formed by winding a thermoplastic resin sheet and a separator, and the roll is held in a pressurized inert gas atmosphere so that the inert gas is supplied to the thermoplastic resin sheet. Contain.
Examples of the inert gas include helium, nitrogen, carbon dioxide, argon, and compressed air. The inert gas permeation time and the inert gas permeation amount until the thermoplastic resin is saturated vary depending on the type of thermoplastic resin to be foamed, the type of inert gas, the permeation pressure, and the thickness of the sheet.

なお、熱可塑性樹脂シートとセパレーターからなるロールを、加圧不活性ガス雰囲気中に保持して該熱可塑性樹脂シートに不活性ガスを含有させる前に、有機溶剤に含有させてもよい。
有機溶剤としては、ベンゼン、トルエン、メチルエチルケトン、ギ酸エチル、アセトン、酢酸、ジオキサン、m−クレゾール、アニリン、アクリロニトリル、フタル酸ジメチル、ニトロエタン、ニトロメタン、ベンジルアルコールなどが挙げられる。これらのうち、取り扱い性および経済性の観点からアセトンがより好ましい。
In addition, you may make it contain in the organic solvent before hold | maintaining the roll which consists of a thermoplastic resin sheet and a separator in a pressurization inert gas atmosphere, and making this thermoplastic resin sheet contain an inert gas.
Examples of the organic solvent include benzene, toluene, methyl ethyl ketone, ethyl formate, acetone, acetic acid, dioxane, m-cresol, aniline, acrylonitrile, dimethyl phthalate, nitroethane, nitromethane, and benzyl alcohol. Of these, acetone is more preferable from the viewpoints of handleability and economy.

熱可塑性樹脂がポリエチレンテレフタレートである場合は、不活性ガスを含有させた後の熱可塑性ポリエステル樹脂シートの結晶化度が30%以上であることが好ましい。結晶化度が30%以上であれば、より均一で微細な気泡が得られる。   When the thermoplastic resin is polyethylene terephthalate, it is preferable that the degree of crystallinity of the thermoplastic polyester resin sheet after containing the inert gas is 30% or more. If the crystallinity is 30% or more, more uniform and fine bubbles can be obtained.

本発明の第2工程では、第1工程を経て不活性ガスが含有された熱可塑性樹脂シートを常圧下で加熱することにより発泡させる。この工程における加熱手段としては、熱風循環式発泡炉、オイルバス、溶融塩バスなどが挙げられる。 In the second step of the present invention, the thermoplastic resin sheet containing the inert gas through the first step is foamed by heating under normal pressure. Examples of the heating means in this step include a hot air circulation type foaming furnace, an oil bath, a molten salt bath, and the like.

より具体的には、例えば、圧力容器からロールを取り出し、熱可塑性樹脂シートとセパレーターとを分離しながら、樹脂シートだけを熱風循環式発泡炉中を通過させる方法が用いられる。発泡条件は、熱可塑性樹脂の軟化温度以上に設定する。その後、炉から出た発泡シートを直ちに成形ロールで平らに成形する。 More specifically, for example, a method is used in which a roll is taken out from the pressure vessel and only the resin sheet is passed through a hot-air circulating foaming furnace while separating the thermoplastic resin sheet and the separator. The foaming conditions are set to be equal to or higher than the softening temperature of the thermoplastic resin. Thereafter, the foamed sheet coming out of the furnace is immediately formed flat with a forming roll.

本発明の第3工程では、第1工程および第2工程を経て発泡された熱可塑性樹脂シートを少なくとも1軸に延伸する。2軸延伸を行う場合には、逐次2軸配向延伸、同時2軸配向延伸、それらを組み合わせた延伸のいずれであっても良い。さらに、延伸は一段延伸でも良いが、多段延伸であっても良い。延伸は熱可塑性樹脂のガラス転移温度以上、融解温度以下の温度で行うことが好ましい。例えば、熱可塑性樹脂がポリエチレンテレフタレートの場合は、延伸は70〜220℃、好ましくは80〜200℃で行うことが好ましい。また、延伸後に熱可塑性樹脂発泡体シートに熱処理を施して熱固定しても良い。熱処理を施す場合の温度は、一般に熱可塑性樹脂のガラス転移温度以上融点以下で行うが、最終的に製品として求められる各種特性を満たすように適宜条件設定される。   In the third step of the present invention, the thermoplastic resin sheet foamed through the first step and the second step is stretched at least uniaxially. In the case of performing biaxial stretching, any of sequential biaxially oriented stretching, simultaneous biaxially oriented stretching, and stretching combining them may be used. Further, the stretching may be single-stage stretching or multi-stage stretching. The stretching is preferably performed at a temperature not lower than the glass transition temperature of the thermoplastic resin and not higher than the melting temperature. For example, when the thermoplastic resin is polyethylene terephthalate, the stretching is preferably performed at 70 to 220 ° C, preferably 80 to 200 ° C. Further, after stretching, the thermoplastic resin foam sheet may be heat-set by heat treatment. The temperature for the heat treatment is generally from the glass transition temperature of the thermoplastic resin to the melting point or less, but is appropriately set so as to satisfy various properties finally required as a product.

延伸の方法は特に限定されないが、一例として、テンター法により、所定の倍率だけ延伸する方法が挙げられる。このとき延伸倍率は特に限定されないが、例えば熱可塑性樹脂がポリエチレンテレフタレートの場合、1軸延伸の場合は縦方向に、2軸延伸の場合は縦方向、横方向それぞれに1.1倍以上5倍未満が好ましい。より好ましくは1.2〜4倍であり、さらに好ましくは1.2〜3倍とする。延伸倍率が1.1倍以上5倍未満であれば、十分な延伸効果が得られるとともに、熱収縮の増大や、引き裂き伝搬抵抗の減少などの問題が生じることもなく、より高反射率の熱可塑性樹脂発泡体を得ることができる。 Although the stretching method is not particularly limited, an example is a method of stretching by a predetermined ratio by a tenter method. At this time, the draw ratio is not particularly limited. For example, when the thermoplastic resin is polyethylene terephthalate, it is 1.1 times or more in the longitudinal direction in the case of uniaxial stretching, 1.1 times or more in the longitudinal direction or in the transverse direction in the case of biaxial stretching. Less than is preferable. More preferably, it is 1.2 to 4 times, and further preferably 1.2 to 3 times. If the draw ratio is 1.1 times or more and less than 5 times, a sufficient drawing effect can be obtained, and there is no problem such as an increase in thermal shrinkage or a decrease in tear propagation resistance, and a heat with higher reflectivity. A plastic resin foam can be obtained.

さらに本発明で得られる熱可塑性樹脂発泡体の発泡倍率は、特に限定されないが、2倍以上であることが好ましい。より好ましくは、2.5倍以上、さらに好ましくは3倍以上である。特に熱可塑性樹脂発泡体の発泡倍率が1.3倍以下の場合は気泡分布が疎になりやすく、結果的に反射率の低下を招きやすくなる。発泡倍率が2倍以上であれば、軽量化の効果があり、折り曲げや打ち抜きなどの2次加工の際に、折り曲げ戻り、抜き不良などが起こり難く生産性が優れる。   Further, the expansion ratio of the thermoplastic resin foam obtained in the present invention is not particularly limited, but is preferably 2 times or more. More preferably, it is 2.5 times or more, more preferably 3 times or more. In particular, when the foaming ratio of the thermoplastic resin foam is 1.3 times or less, the bubble distribution tends to be sparse, and as a result, the reflectance tends to decrease. When the expansion ratio is 2 times or more, there is an effect of reducing the weight, and in the secondary processing such as bending and punching, folding back and defective punching hardly occur and the productivity is excellent.

本発明で得られる熱可塑性樹脂発泡体の厚みは、特に限定されないが、250μm以上であるが好ましい。より好ましくは300μm以上、更に好ましくは350μm以上である。熱可塑性樹脂発泡体の厚みが250μm以上であれば、高反射率を示すとともに、形状保持性、2次加工性、組み込み作業性が優れる。   The thickness of the thermoplastic resin foam obtained in the present invention is not particularly limited, but is preferably 250 μm or more. More preferably, it is 300 micrometers or more, More preferably, it is 350 micrometers or more. When the thickness of the thermoplastic resin foam is 250 μm or more, it exhibits high reflectivity and is excellent in shape retention, secondary workability, and assembly workability.

本発明で得られる熱可塑性樹脂発泡体の400nmから700nmの波長域の光の平均反射率は、90%以上であることが好ましい。より好ましくは、95%以上、更に好ましくは97%以上、特に好ましくは98%以上である。反射率が90%を下回る場合、光反射板として要求される反射特性を十分満たさず、結果的に光反射板を組み込んだ製品として十分な輝度向上効果が得られない傾向があるため好ましくない。   The average reflectance of light in the wavelength region of 400 nm to 700 nm of the thermoplastic resin foam obtained in the present invention is preferably 90% or more. More preferably, it is 95% or more, more preferably 97% or more, and particularly preferably 98% or more. When the reflectance is less than 90%, the reflection characteristics required as a light reflecting plate are not sufficiently satisfied, and as a result, a sufficient brightness improvement effect as a product incorporating the light reflecting plate tends not to be obtained.

本発明で得られる熱可塑性樹脂発泡体の表面光沢度は、特に限定されないが、50%以上であることが好ましい。より好ましくは60%以上、更に好ましくは65%以上である。表面光沢度が50%以上であれば、拡散反射成分が少なくなるため、特にバックライトに使用した場合に、前面に反射される光が多くなり、輝度がより向上する傾向にある。   The surface glossiness of the thermoplastic resin foam obtained in the present invention is not particularly limited, but is preferably 50% or more. More preferably, it is 60% or more, More preferably, it is 65% or more. When the surface glossiness is 50% or more, the diffuse reflection component is reduced, and particularly when used for a backlight, the amount of light reflected on the front surface increases, and the luminance tends to be further improved.

本発明において用いられる熱可塑性樹脂は特に限定されないが、ポリエチレン、ポリプロピレン、ポリスチレン、ポリ塩化ビニル、ポリ塩化ビフェニル、ポリエチレンテレフタレート、ポリビニルアルコールなどの汎用樹脂、ポリカーボネート、ポリブチレンテレフタレート、ポリアミド、ポリアセタール、ポリフェニレンエーテル、超高分子量ポリエチレン、ポリサルフォン、ポリエーテルサルフォン、ポリフェニレンサルファイド、ポリアリレート、ポリアミドイミド、ポリエーテルイミド、ポリエーテルエーテルケトン、ポリイミド、ポリテトラフルオロエチレン、液晶ポリマー、フッ素樹脂などのエンジニアリングプラスチック、またはこれらの共重合体もしくは混合物などが挙げられる。これらのうちでも、耐熱性、耐衝撃性などが良好であることから、ポリエステル、ポリカーボネート、ポリサルフォン、ポリエーテルサルフォン、ポリフェニレンサルファイド、ポリエーテルイミド、シクロポリオレフィンが好ましく、中でもポリエステルが特に好ましい。さらに、ポリエステルの中でも、ポリエチレンテレフタレートが特に好ましい。   The thermoplastic resin used in the present invention is not particularly limited, but is a general-purpose resin such as polyethylene, polypropylene, polystyrene, polyvinyl chloride, polychlorinated biphenyl, polyethylene terephthalate, polyvinyl alcohol, polycarbonate, polybutylene terephthalate, polyamide, polyacetal, polyphenylene ether. , Engineering plastics such as ultrahigh molecular weight polyethylene, polysulfone, polyethersulfone, polyphenylene sulfide, polyarylate, polyamideimide, polyetherimide, polyetheretherketone, polyimide, polytetrafluoroethylene, liquid crystal polymer, fluororesin, or these Or a copolymer thereof. Among these, polyester, polycarbonate, polysulfone, polyethersulfone, polyphenylene sulfide, polyetherimide, and cyclopolyolefin are preferable because of good heat resistance and impact resistance, and polyester is particularly preferable. Furthermore, among polyesters, polyethylene terephthalate is particularly preferable.

本発明において、特性に影響を及ぼさない範囲で、発泡前の熱可塑性樹脂に、結晶化核剤、結晶化促進剤、気泡化核剤、酸化防止剤、帯電防止剤、紫外線防止剤、光安定剤、蛍光増白剤、顔料、染料、相溶化剤、滑剤、強化剤、難燃剤、架橋剤、架橋助剤、可塑剤、増粘剤、減粘剤などの各種添加剤を配合しても良い。また、得られた熱可塑性樹脂発泡体に上記添加剤を含有する樹脂を積層しても良いし、上記添加剤を含有する塗料をコーティングしても良い。 In the present invention, to the thermoplastic resin before foaming, the crystallization nucleating agent, the crystallization accelerator, the bubbling nucleating agent, the antioxidant, the antistatic agent, the ultraviolet ray preventing agent, the light stabilizing agent, as long as the properties are not affected. Various additives such as additives, fluorescent brighteners, pigments, dyes, compatibilizers, lubricants, reinforcing agents, flame retardants, cross-linking agents, cross-linking aids, plasticizers, thickeners, thickeners, etc. good. Moreover, the resin containing the said additive may be laminated | stacked on the obtained thermoplastic resin foam, and the coating material containing the said additive may be coated.

以下に本発明を実施例によって説明するが、本発明は下記例に限定されるものではない。なお、得られた熱可塑性樹脂発泡体の各種特性の測定及び評価は以下の通りとした。
(密度)
熱可塑性発泡体の密度(ρf)は、電子天秤(METTLER社製 AE240)を用いて、水置換法により求めた。
(発泡倍率)
発泡体シートの密度(ρf)を水中置換法により測定し、発泡前の樹脂の密度(ρs)との比ρs/ρfとして算出した。ただし、熱可塑性樹脂がポリエチレンテレフタレートの場合、ρsは1.34として計算した。
(厚さ)
得られた熱可塑性樹脂発泡体の幅方向5点の厚みをTeclock社 SM−112(測定子形状Φ10mm、測定力2.5N以下)を用いて測定し、その平均値を熱可塑性樹脂発泡体の厚みとした。
(反射率)
分光光度計(UV−3101PC:島津製作所製)を用いて、400〜700nmの光の波長域における反射率を測定し、得られたチャートより1nm間隔で反射率を読み取り、平均値を計算した。なお、表1において、硫酸バリウムの微粉末を固めた白板の拡散反射率を100%として、各々の熱可塑性樹脂発泡体の拡散反射率を相対値で示している。
(白色度)
JIS−L−1015に準じて求めた。すなわち、分光光度計(UV−3101PC:島津製作所製)を用いて測定した450nmおよび550nmの波長における反射率をそれぞれB%、G%としたとき、下記式に代入して白色度を求めた。
白色度=4B−3G
(表面光沢度)
表面光沢度は、光沢度計(ミノルタ製 GM−268)により、入射角度60°、受光角度60°で測定した。測定は、すべて試料数n=5で行い、その平均値を求めた。
(形状保持性)
得られた熱可塑性樹脂発泡体を真空成形機により図1に示すような開口部の直径100mm、深さ70mmの半球状の光反射板を熱成形加工した。得られた光反射板を手で持って力を加えて変形の有無を観察し、形状保持性を評価した。
EXAMPLES The present invention will be described below with reference to examples, but the present invention is not limited to the following examples. In addition, the measurement and evaluation of the various characteristics of the obtained thermoplastic resin foam were as follows.
(density)
The density (ρf) of the thermoplastic foam was determined by a water displacement method using an electronic balance (AE240 manufactured by METTER).
(Foaming ratio)
The density (ρf) of the foam sheet was measured by an underwater substitution method and calculated as a ratio ρs / ρf with respect to the density (ρs) of the resin before foaming. However, when the thermoplastic resin was polyethylene terephthalate, ρs was calculated as 1.34.
(thickness)
The thickness of 5 points in the width direction of the obtained thermoplastic resin foam was measured using Teclock SM-112 (measuring element shape Φ10 mm, measuring force 2.5 N or less), and the average value was measured for the thermoplastic resin foam. The thickness was taken.
(Reflectance)
Using a spectrophotometer (UV-3101PC: manufactured by Shimadzu Corporation), the reflectance in the wavelength range of 400 to 700 nm was measured, the reflectance was read at 1 nm intervals from the obtained chart, and the average value was calculated. In Table 1, the diffuse reflectance of each thermoplastic resin foam is shown as a relative value, assuming that the diffuse reflectance of the white plate in which the fine powder of barium sulfate is hardened is 100%.
(Whiteness)
It calculated | required according to JIS-L-1015. That is, when the reflectance at wavelengths of 450 nm and 550 nm measured using a spectrophotometer (UV-3101PC: manufactured by Shimadzu Corporation) was B% and G%, respectively, whiteness was obtained by substituting into the following formula.
Whiteness = 4B-3G
(Surface gloss)
The surface gloss was measured with a gloss meter (GM-268 manufactured by Minolta) at an incident angle of 60 ° and a light receiving angle of 60 °. All measurements were performed with the number of samples n = 5, and the average value was obtained.
(Shape retention)
The resulting thermoplastic resin foam was thermoformed with a vacuum molding machine into a hemispherical light reflector having an opening diameter of 100 mm and a depth of 70 mm as shown in FIG. The obtained light reflection plate was held by hand and force was applied to observe the presence or absence of deformation to evaluate shape retention.

(実施例1)
0.6mm厚×300mm幅×60m長さのポリエチレンテレフタレートシート(C−0312グレード、ユニチカ(株)製)のロールと、セパレーターとして160μm厚さ×290mm幅×60m長さ、目付量55g/m2 のオレフィン系不織布のロール(FT300グレード、日本バイリーン(株)製)とを用意した。両者を重ねて、ポリエチレンテレフタレートシートの表面どうしが接触する部分がないように巻いて新たにロールを作製した。
Example 1
A roll of polyethylene terephthalate sheet (C-0312 grade, manufactured by Unitika Co., Ltd.) having a thickness of 0.6 mm × 300 mm width × 60 m and a separator having a thickness of 160 μm thickness × 290 mm width × 60 m length and a basis weight of 55 g / m 2 An olefin-based non-woven roll (FT300 grade, manufactured by Nippon Vilene Co., Ltd.) was prepared. The rolls were overlapped and wound so that there was no portion where the surfaces of the polyethylene terephthalate sheet contacted each other, and a new roll was produced.

その後、このロールを圧力容器に入れ、炭酸ガスで6MPaに加圧し、ポリエチレンテレフタレートシートに炭酸ガスを浸透させた。ポリエチレンテレフタレートシートへの炭酸ガスの浸透時間は72時間とした。 Then, this roll was put into a pressure vessel, pressurized to 6 MPa with carbon dioxide gas, and carbon dioxide gas was infiltrated into the polyethylene terephthalate sheet. The carbon dioxide gas permeation time into the polyethylene terephthalate sheet was 72 hours.

次に、圧力容器からロールを取り出し、セパレーターを取り除きながら炭酸ガスが浸透したポリエチレンテレフタレートシートだけを220℃に設定した熱風循環式発泡炉に発泡時間が1分となるように連続的に供給して発泡した。得られた発泡体の厚さは1000μm、平均気泡径は9μmであった。 Next, the roll is taken out from the pressure vessel, and only the polyethylene terephthalate sheet infiltrated with carbon dioxide gas is continuously supplied to a hot-air circulating foaming furnace set at 220 ° C. so that the foaming time is 1 minute while removing the separator. Foamed. The obtained foam had a thickness of 1000 μm and an average cell diameter of 9 μm.

次いで、このシートをテンター法延伸装置を用いて180℃にて、延伸倍率が2.0倍となるように1軸方向に延伸し、そのまま200℃にて熱処理をした後、室温まで徐冷した。
延伸した発泡体は、延伸前の厚みに対して35%まで薄肉化したにも関わらず、反射率が、従来の方法では考えられなかった101.1%という値を示した。白色度は107.5であった。得られた結果を表1に示す。
Next, the sheet was stretched in a uniaxial direction at 180 ° C. using a tenter method stretching apparatus so that the stretching ratio was 2.0 times, heat-treated at 200 ° C. as it was, and then gradually cooled to room temperature. .
Although the stretched foam was thinned to 35% of the thickness before stretching, the reflectivity showed a value of 101.1%, which could not be considered by the conventional method. The whiteness was 107.5. The obtained results are shown in Table 1.

(実施例2)
延伸倍率を1.4倍で行った以外は、実施例1と同条件とした。得られた結果を表1に示す。
(Example 2)
The conditions were the same as in Example 1 except that the draw ratio was 1.4. The obtained results are shown in Table 1.

(実施例3)
延伸倍率を2.4倍で行った以外は、実施例1と同条件とした。得られた結果を表1に示す。
(Example 3)
The conditions were the same as in Example 1 except that the draw ratio was 2.4 times. The obtained results are shown in Table 1.

(実施例4)
延伸温度を200℃、延伸倍率を2.5倍で行った以外は、実施例1と同条件とした。得られた結果を表1に示す。
延伸した発泡体は、延伸前の厚みに対比して32%と薄肉化したにも関わらず、反射率が、従来の方法では考えられなかった102.7%という値を示した。白色度は110.9であった。得られた結果を表1に示す。
Example 4
The conditions were the same as in Example 1 except that the stretching temperature was 200 ° C. and the stretching ratio was 2.5 times. The obtained results are shown in Table 1.
The stretched foam showed a value of 102.7%, which was unthinkable by the conventional method, although the thickness was reduced to 32% compared to the thickness before stretching. The whiteness was 110.9. The obtained results are shown in Table 1.

(実施例5)
延伸温度を80℃、延伸倍率を1.5倍で行った以外は、実施例1と同条件とした。得られた結果を表1に示す。
(Example 5)
The conditions were the same as in Example 1 except that the drawing temperature was 80 ° C. and the draw ratio was 1.5 times. The obtained results are shown in Table 1.

(実施例6)
延伸方向を2軸、延伸温度を180℃、延伸倍率を縦方向1.4倍、横方向1.4倍で行った以外は、実施例1と同条件とした。得られた結果を表1に示す。
(Example 6)
The conditions were the same as in Example 1, except that the stretching direction was biaxial, the stretching temperature was 180 ° C., the stretching ratio was 1.4 times in the longitudinal direction, and 1.4 times in the transverse direction. The obtained results are shown in Table 1.

(実施例7)
延伸方向を2軸、延伸温度を100℃、延伸倍率を縦方向1.6倍、横方向1.6倍で行った以外は、実施例1と同条件とした。得られた結果を表1に示す。
(Example 7)
The conditions were the same as in Example 1 except that the stretching direction was biaxial, the stretching temperature was 100 ° C., the stretching ratio was 1.6 times in the longitudinal direction, and 1.6 times in the transverse direction. The obtained results are shown in Table 1.

(比較例1)
延伸行程を行わなかったこと、0.33mm厚×300mm幅×60m長さのポリエチレンテレフタレートシートを用いたこと以外は、実施例1と同条件とした。得られた結果を表1に示す。
得られたシートは、厚みが470μm、反射率が96.6%、白色度が98.8であった。
(Comparative Example 1)
The conditions were the same as in Example 1 except that the stretching process was not performed and a polyethylene terephthalate sheet having a length of 0.33 mm thickness × 300 mm width × 60 m was used. The obtained results are shown in Table 1.
The obtained sheet had a thickness of 470 μm, a reflectance of 96.6%, and a whiteness of 98.8.

Figure 2006095944
Figure 2006095944

本発明の実施例において作製した光反射板を示す断面図Sectional drawing which shows the light reflecting plate produced in the Example of this invention

符号の説明Explanation of symbols

1 熱可塑性樹脂発泡体 1 Thermoplastic foam

Claims (4)

熱可塑性樹脂シートを加圧不活性ガス雰囲気中に保持して不活性ガスを含有させる工程と、不活性ガスを含有させた熱可塑性樹脂シートを常圧下で加熱して発泡させる工程と、発泡した熱可塑性樹脂シートを少なくとも1軸に延伸させる工程とからなる製造方法により製造された熱可塑性樹脂発泡体。 The step of holding the thermoplastic resin sheet in a pressurized inert gas atmosphere to contain an inert gas, the step of heating and foaming the thermoplastic resin sheet containing the inert gas under normal pressure, and foaming A thermoplastic resin foam produced by a production method comprising a step of stretching a thermoplastic resin sheet at least uniaxially. 前記熱可塑性樹脂発泡体の発泡倍率が2倍以上であり、かつ、前記熱可塑性樹脂発泡体のシートの厚さが250μm以上であることを特徴とする請求項1に記載の熱可塑性樹脂発泡体。 2. The thermoplastic resin foam according to claim 1, wherein a foaming ratio of the thermoplastic resin foam is 2 times or more and a thickness of the thermoplastic resin foam sheet is 250 μm or more. . 400〜700nmの光の波長域における平均反射率が90%以上であることを特徴とする請求項1または2に記載の熱可塑性樹脂発泡体。 The thermoplastic resin foam according to claim 1 or 2, wherein an average reflectance in a wavelength range of 400 to 700 nm is 90% or more. 前記熱可塑性樹脂がポリエステルであることを特徴とする請求項1乃至3のいずれか1項に記載の熱可塑性樹脂発泡体。

The thermoplastic resin foam according to any one of claims 1 to 3, wherein the thermoplastic resin is polyester.

JP2004286602A 2004-09-30 2004-09-30 Thermoplastic resin foam Pending JP2006095944A (en)

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Cited By (6)

* Cited by examiner, † Cited by third party
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WO2008053740A1 (en) * 2006-10-27 2008-05-08 Toray Industries, Inc. White polyester film for liquid crystal display reflector
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JP2009244749A (en) * 2008-03-31 2009-10-22 Furukawa Electric Co Ltd:The Light reflective plate
JP2010271694A (en) * 2009-04-23 2010-12-02 Furukawa Electric Co Ltd:The Light diffusing foamed sheet and method of manufacturing the same, backlight device, and illumination device
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WO2008053740A1 (en) * 2006-10-27 2008-05-08 Toray Industries, Inc. White polyester film for liquid crystal display reflector
EP2077458A1 (en) * 2006-10-27 2009-07-08 Toray Industries, Inc. White polyester film for light reflective plate
EP2077458A4 (en) * 2006-10-27 2012-03-28 Toray Industries White polyester film for light reflective plate
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JP2010271694A (en) * 2009-04-23 2010-12-02 Furukawa Electric Co Ltd:The Light diffusing foamed sheet and method of manufacturing the same, backlight device, and illumination device

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