JP2000328230A - Method for deposition of organic film - Google Patents
Method for deposition of organic filmInfo
- Publication number
- JP2000328230A JP2000328230A JP11139769A JP13976999A JP2000328230A JP 2000328230 A JP2000328230 A JP 2000328230A JP 11139769 A JP11139769 A JP 11139769A JP 13976999 A JP13976999 A JP 13976999A JP 2000328230 A JP2000328230 A JP 2000328230A
- Authority
- JP
- Japan
- Prior art keywords
- film
- organic
- substrate
- forming
- group
- 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
Landscapes
- Surface Treatment Of Optical Elements (AREA)
- Application Of Or Painting With Fluid Materials (AREA)
- Materials Applied To Surfaces To Minimize Adherence Of Mist Or Water (AREA)
- Paints Or Removers (AREA)
- Physical Vapour Deposition (AREA)
Abstract
Description
【0001】[0001]
【発明の属する技術分野】本発明は、有機ポリシロキサ
ン系化合物またはパーフルオロアルキル基含有化合物を
含む有限量の有機系物質を加熱蒸発させ、物品に膜付け
をする有機膜の成膜法に関するものである。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for forming an organic film by heating and evaporating a finite amount of an organic material containing an organic polysiloxane compound or a compound containing a perfluoroalkyl group, thereby forming a film on an article. It is.
【0002】本発明はまた、主に、物品に滑り性機能、
撥水性機能、汚れ防止機能などを付与する、特に物品の
外観を損なうことなく薄い膜を物品に付与する成膜法に
関するものである。[0002] The present invention also relates mainly to the use of a slip function on an article,
The present invention relates to a film-forming method for imparting a water-repellent function, a stain-preventing function, etc., and in particular for imparting a thin film to an article without impairing the appearance of the article.
【0003】本発明はまた、各種表示画面の最表面、あ
るいは各種表示画面の前面に用いられる光学フィルター
の最表面、めがねレンズなどの最表面に用いられる膜、
特に反射防止機能膜の最表面に付与する膜の成膜法に関
するものである。The present invention also relates to a film used on the outermost surface of various display screens, the outermost surface of an optical filter used in front of various display screens, the outermost surface of an eyeglass lens or the like,
In particular, the present invention relates to a method for forming a film to be provided on the outermost surface of the antireflection function film.
【0004】[0004]
【従来の技術】従来、成膜対象基材に、有機ポリシロキ
サン系化合物またはパーフルオロアルキル基含有化合物
を含む膜を膜付けする方法として、浸漬塗装、スピン塗
装、カーテン塗装、ロール転写塗装、グラビア印刷に代
表される印刷手法などの溶液塗布法、真空蒸着、イオン
プレーティング、およびスパッタリング手法などのドラ
イ手法が用いられてきた。2. Description of the Related Art Hitherto, as a method of applying a film containing an organic polysiloxane compound or a compound containing a perfluoroalkyl group to a substrate to be formed on a film, dip coating, spin coating, curtain coating, roll transfer coating, gravure, and the like are known. A solution coating method such as a printing method represented by printing, a dry method such as a vacuum deposition, an ion plating, and a sputtering method have been used.
【0005】上記の浸漬塗装については、特開昭62−
148902号公報などに記載されているが、溶液の粘
度などにより、該化合物を含有する膜の膜厚を厳密に制
御するのは難しかった。膜が薄すぎると滑り性機能、撥
水性の機能、汚れ防止機能などが十分に発揮されず、反
対に膜が厚すぎると膜の耐久性に問題が生じたり、膜の
表面を擦ると膜がとれてしまうという問題も生じた。[0005] The above dip coating is disclosed in
Although described in 148902, it is difficult to strictly control the thickness of the film containing the compound depending on the viscosity of the solution. If the film is too thin, the slippery function, water repellent function, stain prevention function, etc. will not be sufficiently exhibited.On the other hand, if the film is too thick, there will be a problem with the durability of the film, or if the surface of the film is rubbed, the film will be damaged. There was also the problem of being taken off.
【0006】また、ドライ手法については、特開平4−
72055号公報などに記載されているが、有機物系の
被膜形成物質が真空蒸着法でごく薄く成膜されている
が、成膜された膜の厚さについては、結果として0.0
3マイクロメートルになるという、薄膜の厚さを制御で
きるものではなかった。従って、実際に撥水性や汚れ防
止性の機能を十分に満たす膜かどうかは、できたものを
真空容器から取り出し評価するしかなかった。実際に
は、有機物が蒸発するとその沸騰あるいは昇華により真
空室の圧力が上昇するが、この圧力上昇の程度を見て有
限量の量を決めたり、加熱源の上部のシャッター板を開
閉したりして行ってきた。この場合、膜が薄すぎて本来
の機能が発揮されなかったり膜が厚すぎて表面を擦ると
膜が剥がれ白っぽくなって汚れてしまうという問題が発
生した。[0006] Regarding the dry method, see Japanese Unexamined Patent Publication No.
No. 72055, etc., an organic film-forming substance is formed very thinly by a vacuum evaporation method, and as a result, the thickness of the formed film is 0.0
It was not possible to control the thickness of the thin film to be 3 micrometers. Therefore, to determine whether or not the film actually satisfies the functions of water repellency and antifouling property, it was necessary to take out the resulting film from the vacuum vessel and evaluate it. In practice, when the organic matter evaporates, the pressure in the vacuum chamber rises due to its boiling or sublimation.However, by observing the degree of this pressure increase, a finite amount is determined, or the shutter plate above the heating source is opened and closed. I went. In this case, there has been a problem that the film is too thin to perform its intended function, or the film is too thick to rub the surface, causing the film to peel off, become whitish, and become dirty.
【0007】また、有機ポリシロキサン系化合物または
パーフルオロアルキル基含有化合物を含む有限量の有機
系物質を、せいぜい100nm以下であるように、ごく薄
く成膜する場合、その蒸発自体をコントロールさせるこ
とは行われていなかった。When a finite amount of an organic substance containing an organic polysiloxane compound or a perfluoroalkyl group-containing compound is formed as a very thin film having a thickness of 100 nm or less at most, it is difficult to control the evaporation itself. Had not been done.
【0008】一方、有機ポリシロキサン系化合物または
パーフルオロアルキル基含有化合物を含む有機系物質で
はないが、ドライ手法の中で有機膜の蒸発をコントロー
ルする手法としては、特開昭63−270456号公報
に記載されている様に、クヌードセンセルの温度を一定
にするような温度コントロールはなされてきた。しかし
ながら、これは有機物の蒸発現象を温度によってコント
ロールするための制御であり、蒸発量あるいは蒸発され
た膜の膜厚を制御するものではなかった。従って、滑り
性機能、撥水性機能膜あるいは汚れ防止機能膜などの場
合のように成膜された膜厚によってその機能が果たされ
るものに関してその機能を制御するものではなかった。On the other hand, although it is not an organic substance containing an organic polysiloxane compound or a compound containing a perfluoroalkyl group, a method for controlling evaporation of an organic film in a dry method is disclosed in JP-A-63-270456. Temperature control has been performed to keep the temperature of the Knudsen cell constant, as described in US Pat. However, this is a control for controlling the evaporation phenomenon of the organic matter by the temperature, and does not control the amount of evaporation or the thickness of the evaporated film. Therefore, the function is not controlled with respect to the function that is performed by the formed film thickness as in the case of the slipperiness function, the water repellency function film, the stain prevention function film, and the like.
【0009】[0009]
【発明が解決しようとする課題】本発明者は、上記の問
題点を解決するために鋭意検討した結果、以下に述べる
本発明に到達した。The present inventors have made intensive studies to solve the above-mentioned problems, and as a result, have reached the present invention described below.
【0010】本発明の目的は、真空蒸着法のようなドラ
イプロセスにおいて、有機ポリシロキサン系化合物また
はパーフルオロアルキル基含有化合物を含む有限量の有
機系物質を加熱蒸発させ、物品の表面に成膜し、滑り性
機能や撥水性機能や汚れ防止機能などを持たせる場合
に、膜厚を好適に制御するとともに、さらに、安定的に
失敗無く、その再現性を実現し、かつその機能を必要十
分に満たす有機膜の成膜法を提供することにある。An object of the present invention is to form a film on the surface of an article by heating and evaporating a finite amount of an organic substance containing an organic polysiloxane compound or a compound containing a perfluoroalkyl group in a dry process such as a vacuum evaporation method. In addition, when providing a slip function, water repellency function, dirt prevention function, etc., properly control the film thickness, stably realize the reproducibility without failure, and make the function necessary and sufficient It is an object of the present invention to provide a method for forming an organic film satisfying the following conditions.
【0011】[0011]
【課題を解決するための手段】本発明の有機膜の製膜法
は、上記目的を解決するため下記の構成からなる。Means for Solving the Problems A method for forming an organic film according to the present invention has the following constitution to solve the above-mentioned object.
【0012】すなわち、本発明の有機膜の成膜法は、成
膜対象基材に、有機ポリシロキサン系化合物またはパー
フルオロアルキル基含有化合物を含む有機系物質を含む
膜を形成する方法において、該有機系物質を加熱蒸発さ
せ、その蒸発量の測定結果をもとに該蒸発量を実質的に
一定にするように加熱源の出力を制御するとともに、該
出力に上限または/および下限を設けることを特徴とす
る有機膜の成膜法である。That is, the method for forming an organic film according to the present invention is a method for forming a film containing an organic substance containing an organic polysiloxane compound or a perfluoroalkyl group-containing compound on a substrate to be formed. Heating and evaporating an organic substance, controlling an output of a heating source so as to keep the evaporation amount substantially constant based on a measurement result of the evaporation amount, and providing an upper limit and / or a lower limit to the output. This is a method for forming an organic film.
【0013】[0013]
【発明の実施の形態】本発明においては、有機ポリシロ
キサン系化合物またはパーフルオロアルキル基含有化合
物を含む有限量の有機系物質を加熱蒸発させ、その蒸発
量を測定し、そしてその測定結果をもとに該蒸発量を実
質的に一定にするように加熱源の出力に上限または/お
よび下限を設けてを制御することによって成膜対象基材
に上記の有機系物質を含む膜を成膜する。DESCRIPTION OF THE PREFERRED EMBODIMENTS In the present invention, a finite amount of an organic substance containing an organic polysiloxane compound or a perfluoroalkyl group-containing compound is heated and evaporated, the amount of evaporation is measured, and the measurement result is also obtained. The upper limit and / or the lower limit are provided to the output of the heating source so as to make the evaporation amount substantially constant, and the film containing the organic substance is formed on the film formation target substrate. .
【0014】本発明の実施において、加熱手段が、蒸発
量がコントロールできる出力をもつ加熱方法としては、
電子銃加熱方式、誘導加熱方式、および光照射方式など
が挙げられるが、抵抗加熱法が最も好ましい。抵抗加熱
方式では上記の有機系物質の急激な突沸などが起こりに
くく都合が良い。さらに抵抗加熱ボートを利用した熱輻
射加熱方式が最も好ましい。この場合さらに突沸の問題
や急激な化合物の分解が発生せず、実際に成膜される膜
特性が加熱する有機系物質で予測できることもあり非常
に有利である。ここでいう抵抗加熱ボートを利用した熱
輻射加熱方式とは、有機系物質と抵抗加熱ボートは接点
をもたず(接触させず)、ある空間を介して抵抗加熱ボ
ートの熱が輻射熱伝達によって伝えられる方式である。
ここで、抵抗加熱方式で使用されるボートの材料として
はモリブデンあるいはタングステンが高融点、耐久性の
面で好ましく用いられる。In the practice of the present invention, the heating means has an output capable of controlling the amount of evaporation.
Examples include an electron gun heating method, an induction heating method, and a light irradiation method, and the resistance heating method is most preferable. In the resistance heating method, rapid bumping or the like of the organic substance is less likely to occur, which is convenient. Further, a heat radiation heating method using a resistance heating boat is most preferable. In this case, the problem of bumping and rapid decomposition of the compound do not occur, and the characteristics of the film actually formed can be predicted by the organic substance to be heated, which is very advantageous. Here, the thermal radiation heating method using a resistance heating boat means that the organic material and the resistance heating boat do not have a contact point (do not contact), and the heat of the resistance heating boat is transmitted through a certain space by radiant heat transfer. This is the method used.
Here, molybdenum or tungsten is preferably used as the material of the boat used in the resistance heating method in terms of high melting point and durability.
【0015】上記有機系物質の蒸発量を測定する手段と
しては、光学式膜厚計、四重極方式の質量分析計、およ
び水晶式膜厚計等による方式が挙げられるが、蒸発源の
出力を制御するためには、非常に微量の質量を測定でき
る必要があるため、水晶式膜厚計が有利である。ここで
いう水晶式膜厚計とは、水晶振動子と呼ばれる水晶に膜
を堆積させその質量の変化を固有振動数の変化から算出
する膜厚計である。通常、金属膜や、金属酸化物系の膜
には汎用されているが、有機膜なかでも有機ポリシロキ
サン系化合物またはパーフルオロアルキル基含有化合物
を含む有限量の有機系物質での適用例は見られない。Means for measuring the evaporation amount of the organic substance include an optical film thickness meter, a quadrupole mass spectrometer, and a quartz crystal film thickness meter. Since it is necessary to measure a very small amount of mass in order to control the thickness, a quartz-type film thickness meter is advantageous. The quartz-type film thickness meter referred to here is a film thickness meter that deposits a film on a crystal called a crystal oscillator and calculates a change in mass from a change in a natural frequency. In general, metal films and metal oxide films are generally used, but among organic films, application examples of a finite amount of organic materials including organic polysiloxane compounds or perfluoroalkyl group-containing compounds have not been seen. I can't.
【0016】このように有機系物質を加熱して蒸発させ
る場合、蒸発潜熱で一旦吸熱挙動が発生したりあるいは
分解熱あるいは解離熱などの挙動が発生したりして、通
常のPID制御(比例、積分、微分制御)でのパラメー
タ調整だけでははうまくコントロールできないことがあ
った。有機系蒸発現象では、線形に温度と蒸気圧の関係
ができないことや、何種類もの有機系物質を混合するた
めに沸点がいくつもあって、挙動が予測できないことも
しばしばあった。When an organic substance is heated and evaporated in this way, endothermic behavior occurs once due to latent heat of evaporation, or behavior such as heat of decomposition or heat of dissociation occurs. In some cases, it was not possible to control well just by adjusting the parameters in the integral and derivative controls. In the organic evaporation phenomenon, the relationship between the temperature and the vapor pressure cannot be linearly determined, and the behavior cannot often be predicted due to the fact that various kinds of organic substances are mixed and thus have many boiling points.
【0017】また、真空蒸着の場合は、蒸発源付近の真
空圧力を一定にすることがなかなか難しく、蒸気圧との
関係でしばしば再現性が得られないことがしばしばあっ
た。さらに有機系物質への加熱が本当に均一でないと、
材料の大きさによる熱容量の問題もあって蒸発が安定的
にある時間持続することが難しいこともあった。In the case of vacuum deposition, it is very difficult to keep the vacuum pressure near the evaporation source constant, and reproducibility is often not obtained due to the relationship with the vapor pressure. Furthermore, if the heating of organic materials is not really uniform,
Due to the heat capacity problem due to the size of the material, it was sometimes difficult to stably evaporate for a certain period of time.
【0018】さらに、蒸発現象をコントロールしてか
ら、膜厚モニタが捕らえる堆積速度に時間遅れが生じ、
瞬間瞬間に起こっている蒸発現象と膜厚モニタで実際に
測定される堆積速度から出される制御信号がマッチしな
いことがしばしばあった。Further, after controlling the evaporation phenomenon, a time delay occurs in the deposition rate captured by the film thickness monitor,
There is often a mismatch between the evaporation phenomenon occurring at the moment and the control signal derived from the deposition rate actually measured by the film thickness monitor.
【0019】そこで、上記出力をPID制御するのに加
えて、その出力に上限あるいは(かつ)下限を用いた。
すると、非常に安定的にかつ失敗無く、再現性のある制
御が可能になった。Therefore, in addition to performing the PID control on the output, an upper limit and / or a lower limit is used for the output.
Then, very stable and reproducible control became possible.
【0020】すなわち、まず、本発明で加熱源への出力
に上限を設けた場合について説明する。That is, first, the case where an upper limit is set for the output to the heating source in the present invention will be described.
【0021】出力一定でモニタ上で堆積速度が上昇始め
てから、目標の速度付近になってくる。蒸発現象が進む
につれ、徐々に堆積速度がそ上昇する。その上昇カーブ
が急激となり、通常のPID制御パラメータで制御して
も加熱源への出力がゼロになるだけでどんどん堆積速度
が上昇し目標速度から大幅にかけ離れてしまう場合があ
る。加熱源への出力に上限を設けておくと目標堆積速度
に到達するまでの時間が若干長くなるが、堆積速度の上
昇カーブを急激化させないで制御できるようになる。上
限の決定方法は、有機系物質の蒸発現象によるが、加熱
限への出力を下側から一定出力で何回かテストする。蒸
発させたときの上記膜厚をモニタで監視し、堆積速度が
目標になったときに出力をゼロにして目標堆積速度×5
倍の堆積速度を超えない出力とすると好ましい。After the deposition speed starts to increase on the monitor at a constant output, it approaches the target speed. As the evaporation phenomenon progresses, the deposition rate gradually increases. The rising curve becomes steep, and even if the control is performed with the normal PID control parameters, the output to the heating source may become zero, but the deposition rate will increase rapidly and may be far away from the target speed. If an upper limit is set for the output to the heating source, the time required to reach the target deposition rate becomes slightly longer, but the control can be performed without abruptly increasing the deposition rate rise curve. The method of determining the upper limit depends on the evaporation phenomenon of the organic substance, but the output to the heating limit is tested several times at a constant output from below. The film thickness at the time of evaporation is monitored by a monitor, and when the deposition rate reaches the target, the output is set to zero and the target deposition rate × 5
Preferably, the output does not exceed the double deposition rate.
【0022】次に、加熱限への出力に下限を設けた場合
について説明する。Next, a case where a lower limit is set for the output to the heating limit will be described.
【0023】出力一定でモニタ上で堆積速度が上昇始め
てから、目標の速度付近になってくる。蒸発現象が進む
につれ、徐々に堆積速度が上昇する。その後、通常のP
ID制御パラメータで制御すると、目標の堆積速度を超
え徐々に加熱源への出力を下げる。しかしながら上記で
説明した蒸発現象の乱れのためか急激に堆積速度が低下
しどんどん加熱源への出力を上昇させても目標の堆積速
度の10%も満たない状態になってしまう場合がある。
この場合、加熱源への出力に下限を設けておくと制御中
に堆積速度の急激な低下をさけることが可能になる。下
限の決定方法は、有機系物質の蒸発現象によるが、加熱
限への出力を下側から一定出力で何回かテストする。上
記膜厚モニタで監視し、堆積速度が目標になったときに
出力を下げ、ある時間(例えば10秒)経過後に、堆積
速度が目標堆積速度の10%になる、出力とすると好ま
しい。該時間は、堆積速度の応答性を考慮して決定され
ることが好ましい。After the deposition speed starts to increase on the monitor at a constant output, it approaches the target speed. As the evaporation phenomenon progresses, the deposition rate gradually increases. Then, the normal P
When controlled by the ID control parameter, the output to the heating source is gradually reduced beyond the target deposition rate. However, the deposition rate may decrease rapidly due to the disturbance of the evaporation phenomenon described above, and even if the output to the heating source is rapidly increased, the deposition rate may be less than 10% of the target deposition rate.
In this case, if a lower limit is set for the output to the heating source, it is possible to prevent a rapid decrease in the deposition rate during control. The method of determining the lower limit depends on the evaporation phenomenon of the organic substance, but the output to the heating limit is tested several times at a constant output from below. Preferably, the output is monitored by the above film thickness monitor, and the output is reduced when the deposition rate reaches the target, and after a certain time (for example, 10 seconds), the deposition rate becomes 10% of the target deposition rate. The time is preferably determined in consideration of the response of the deposition rate.
【0024】加熱源への出力に上限と下限を組み合わせ
ることも好ましく用いられる。It is also preferable to combine an upper limit and a lower limit with the output to the heating source.
【0025】本発明において、成膜対象基材板に成膜さ
れた膜の膜厚は1nmから30nmであることが非常に好ま
しい。さらに好ましくは、2nm〜10nmであることが非
常に好ましい。これは、目的とする滑り性機能、撥水性
性機能、および汚れ防止性機能を有する場合、1nm以下
になるとその効果が十分に発揮されにくくなり、例えば
撥水性機能を図る尺度として水に対する接触角を測定す
れば判る。また、膜厚が30nmを超えると接触角で評価
すると十分特性は満たしているが、膜が厚膜化しすぎて
いて表面を擦ると膜が剥がれてしまう現象が発生する。
そのため白化したりして汚れ状に見えてしまう。膜厚が
2nm〜10nmであると、目標の特性が安定して得られ
る。In the present invention, the thickness of the film formed on the target substrate plate is very preferably 1 nm to 30 nm. More preferably, it is very preferably from 2 nm to 10 nm. This is because, when it has a desired slip function, water repellency function, and antifouling function, its effect becomes difficult to be sufficiently exhibited when the thickness is 1 nm or less, for example, a contact angle with water as a measure for the water repellency function. You can tell by measuring. When the film thickness exceeds 30 nm, the characteristics are sufficiently satisfied when evaluated by a contact angle, but a phenomenon occurs in which the film is too thick and the film is peeled off when the surface is rubbed.
For this reason, it is whitened and looks dirty. When the film thickness is 2 nm to 10 nm, target characteristics can be stably obtained.
【0026】本発明で用いられる有機系物質は多孔質材
料に保持させていることが好ましい。これは、有機系物
質を均一分散化にして物質として保持でき、さらには、
分散化状態が良ければ加熱がむらなく行われ均一な蒸発
が可能となるためである。液状のまま容器に入れた場合
は、ヒータの近くと蒸発表面に気化現象のばらつきが生
じ、ひいては突沸などの現象も免れなくなる。The organic substance used in the present invention is preferably held on a porous material. This means that organic substances can be uniformly dispersed and retained as a substance.
This is because, if the state of dispersion is good, heating is performed evenly and uniform evaporation is possible. If the liquid is put in a container in a liquid state, the vaporization phenomenon varies near the heater and on the evaporation surface, and the phenomenon such as bumping cannot be avoided.
【0027】また、本発明では、有機系物質を繊維状の
導電性物質に付着させて用いることが好ましい。繊維状
の導電性物質表面に有機系物質が付着しているために、
加熱したとき導電性繊維を通して加熱することが可能と
なり有機系物質の均一な加熱が可能となる。ここで導電
性物質としては、耐熱性の高い鉄、アルミニウム、銅ま
たはカーボンが好ましく用いられる。特に市販のスチー
ルウールが安価で取り扱いも容易であり好適である。形
状、線径も特に限定しないが、加工性、熱伝導性、有機
系物質の付着性から線径が0.01mm〜1mmのもの
が好ましくさらに0.025mm〜0.05mmのもの
が最も適当である。Further, in the present invention, it is preferable to use an organic substance by attaching it to a fibrous conductive substance. Because organic substances are attached to the fibrous conductive material surface,
When heated, heating can be performed through the conductive fibers, and uniform heating of the organic material can be performed. Here, as the conductive material, iron, aluminum, copper, or carbon having high heat resistance is preferably used. Particularly, commercially available steel wool is suitable because it is inexpensive and easy to handle. The shape and the wire diameter are not particularly limited, but the wire diameter is preferably 0.01 mm to 1 mm, and more preferably 0.025 mm to 0.05 mm, from the viewpoint of workability, heat conductivity, and adhesion of organic substances. is there.
【0028】本発明においては、導電性物質を少なくと
も一方向が開放している保持枠に入れるとさらに好まし
い。これは、保持枠に入れることで有機系物質が加熱に
より溶融した場合に下に流れでることを防止でき、さら
に真空室下面の汚染防止にもなる。さらにあらゆる方向
に蒸発する向きがあると真空室の壁を汚染する原因とな
るので蒸発する方向を成膜対象基板方向のみ開放するこ
とが好ましい。In the present invention, it is more preferable that the conductive substance is placed in a holding frame that is open in at least one direction. This can prevent the organic substance from flowing downward when the organic substance is melted by heating by being put in the holding frame, and also prevent contamination of the lower surface of the vacuum chamber. Further, if there is a direction in which evaporation occurs in any direction, it may cause the wall of the vacuum chamber to be contaminated. Therefore, it is preferable to open the evaporation direction only to the substrate to be film-formed.
【0029】本発明においては、有機ポリシロキサン系
化合物としては、中でもポリジメチルシロキサン系重合
物が特性上の接触角を大きくすることが可能なことから
好ましく使用される。かかるシロキサンの具体例として
は、末端にシラノール基を有するポリジメチルシロキサ
ン、ポリメチルフェニルシロキサン、ポリメチルビニル
シロキサンなどのポリアルキル、ポリアルケニル、ある
いはポリアリールシロキサンに各種架橋剤、例えばテト
ラアセトキシシラン、テトラアルコキシキシシラン、テ
トラエチルメチルケトオキシムシラン、テトライソプロ
ペニルシランなどの四官能シラン、さらにはアルキルあ
るいはアルケニルトリアセトキシシラン、トリケトオキ
シムシラン、またはトリイソプロペニルシラントリアル
コキシシランなどの3官能シランなどを添加混合したも
の、場合によってはあらかじめ反応させたものが挙げら
れる。In the present invention, as the organic polysiloxane compound, a polydimethylsiloxane polymer is particularly preferably used because it can increase the characteristic contact angle. Specific examples of such siloxanes include polyalkylsiloxanes such as polydimethylsiloxane, polymethylphenylsiloxane, and polymethylvinylsiloxane having a terminal silanol group, polyalkenyl, or polyarylsiloxane, and various crosslinking agents such as tetraacetoxysilane and tetraacetoxysilane. Add tetrafunctional silane such as alkoxyoxysilane, tetraethylmethylketoxime silane, tetraisopropenyl silane, and trifunctional silane such as alkyl or alkenyltriacetoxysilane, triketoxime silane, or triisopropenyl silane trialkoxy silane. Examples of the mixture include those mixed and, in some cases, reacted in advance.
【0030】他のポリシロキサンの例としては、Si−
H結合を有するポリシロキサンと不飽和基を有する化合
物を白金化化合物などの触媒存在下に反応させて硬化さ
せてなる化合物なども挙げることができる。Examples of other polysiloxanes include Si-
Compounds obtained by reacting a polysiloxane having an H bond with a compound having an unsaturated group in the presence of a catalyst such as a platinized compound and curing the compound can also be used.
【0031】パーフルオロアルキル基含有化合物として
は、特に限定されるものではないが、特にパーフルオロ
基含有(メタ)アクリレートを含むポリマーおよび他の
モノマーとの共重合体が好ましい。これらの重合物中に
は架橋硬化せしめる目的で各種の官能基を導入させたも
のが使用されるが、その具体例としてはヒドロキシ(メ
タ)アクリレートなどの水酸基含有モノマー、(メタ)
アクリル酸などのカルボキシル基含有モノマーなどとの
共重合体が挙げられる。さらにはアリル(メタ)アクリ
レートなどの反応性の異なる二重結合を有するモノマー
との共重合体も架橋硬化可能な例として挙げられる。か
かる共重合体の重合形態としては、特に限定されず、ラ
ンダム共重合体、ブロック共重合体等が適用可能でであ
るが、撥水性、成膜対象基板の表面の接着性向上等の点
からブロック共重合体が特に好ましく使用される。The perfluoroalkyl group-containing compound is not particularly limited, but a polymer containing a perfluoro group-containing (meth) acrylate and a copolymer with another monomer are particularly preferable. Among these polymers, those into which various functional groups are introduced for the purpose of crosslinking and curing are used. Specific examples thereof include hydroxyl group-containing monomers such as hydroxy (meth) acrylate, and (meth)
Copolymers with a carboxyl group-containing monomer such as acrylic acid are exemplified. Further, a copolymer with a monomer having a double bond having different reactivity such as allyl (meth) acrylate is also mentioned as an example capable of crosslinking and curing. The polymerization form of such a copolymer is not particularly limited, and random copolymers, block copolymers, and the like can be applied, but from the viewpoint of improving water repellency, adhesion of the surface of the substrate on which a film is to be formed, and the like. Block copolymers are particularly preferably used.
【0032】前述のかかる末端シラノール有機ポリシロ
キサンの分子量は特に限定されないが、安定性、取り扱
いのやすさなどの点から、数平均分子量で好ましくは1
000〜100万、さらに好ましくは2000〜50万
の末端シラノール有機ポリシロキサンが使用される。The molecular weight of the above-mentioned organopolysiloxane having a terminal silanol is not particularly limited, but is preferably 1 in terms of number average molecular weight in terms of stability, ease of handling, and the like.
000 to 1,000,000, more preferably 2000 to 500,000 terminal silanol organopolysiloxanes are used.
【0033】さらにはジメチルジクロルシラン、ジメチ
ルジアルコキシシラン、ジメチルアセトキシシランなど
のモノマーを加水分解して、末端シラノール基を有する
有機ポリシロキサンとすることも可能である。また、さ
らに縮合反応を進行させて、前述の末端シラノール基を
有する有機ポリシロキサンとすることも可能である。Further, it is also possible to hydrolyze monomers such as dimethyldichlorosilane, dimethyldialkoxysilane and dimethylacetoxysilane to obtain an organic polysiloxane having a terminal silanol group. Further, it is possible to further advance the condensation reaction to obtain the above-mentioned organopolysiloxane having a terminal silanol group.
【0034】以上の有機系物質を含む組成物中には、硬
化を促進させる目的、あるいは硬化可能ならしめる目的
から各種硬化剤、3次元架橋剤を添加することも可能で
ある。これらの具体例としてはシリコーン樹脂硬化剤、
シランカップリング剤、各種金属アルコレート、各種金
属キレート化合物、イソシアネート化合物、メラミン樹
脂、多官能アクリル樹脂、あるいは尿素樹脂などがあ
る。Various curing agents and three-dimensional crosslinking agents can be added to the composition containing the above-mentioned organic substance for the purpose of accelerating curing or making the composition curable. Examples of these are silicone resin curing agents,
Examples include silane coupling agents, various metal alcoholates, various metal chelate compounds, isocyanate compounds, melamine resins, polyfunctional acrylic resins, and urea resins.
【0035】さらに具体的な例として、本発明で用いら
れる有機系物質は、下式(I)で示される化合物を含む
ことが簡易で好ましい。As a more specific example, it is simple and preferable that the organic substance used in the present invention contains a compound represented by the following formula (I).
【0036】 n−CpFp+1CH2CH2Si(NH2)3 ・・・(I) (ただし、pは自然数) 例えば、3,3,3−トリフルオロプロピルトリアミノ
シラン、2−(パーフルオロプロピル)エチルトリアミ
ノシラン、2−(パーフルオロブチル)エチルトリアミ
ノシラン、(パーフルオロヘキシル)エチルトリアミノ
シラン、2−(パーフルオロオクチル)エチルトリアミ
ノシランなどのが化合物を単独はもちろん2種以上を混
合して用いることもできる。N—C p F p + 1 CH 2 CH 2 Si (NH 2 ) 3 ... (I) (where p is a natural number) For example, 3,3,3-trifluoropropyltriaminosilane, 2- Compounds such as (perfluoropropyl) ethyltriaminosilane, 2- (perfluorobutyl) ethyltriaminosilane, (perfluorohexyl) ethyltriaminosilane, and 2- (perfluorooctyl) ethyltriaminosilane may be used alone or in combination of two or more. Can also be used as a mixture.
【0037】さらに滑り性や汚れ防止機能としての指紋
などのふき取り性を良くするものとして、該有機系物質
が下式(II)で示され、数平均分子量が500から10
000であるケイ素含有有機含有フッ素化合物を含むこ
とを特徴とすることが好ましく用いられる。The organic substance is represented by the following formula (II) and has a number average molecular weight of 500 to 10 to further improve the slipping property and the wiping property of a fingerprint or the like as a function of preventing contamination.
It is preferably used that it contains a silicon-containing organic-containing fluorine compound of 000.
【0038】[0038]
【化2】 (式中、Rfは、パーフルオロアルキル基を表す。Z
は、フッ素またはトリフルオロメチル基を表す。a,b,c,
d,eは、それぞれ独立して、0または1以上の整数を表
し、a+b+c+d+eは、少なくとも1以上であり、a,b,c,d,e
でくくられた繰り返し単位の存在順序は、式中において
限定されない。Yは、水素又は炭素数1〜4のアルキル
基を表す。Xは、水素、臭素又はヨウ素を表す。R
1は、水酸基又は加水分解可能な置換基を表す。R2は、
水素又は1価の炭化水素基を表す。lは、0、1又は2
を表す。mは、1、2又は3を表す。) さらに滑り性や汚れ防止機能としての指紋などのふき取
り性を良くするものとして、本発明では、有機系物質が
下式(III)で示される末端にカルバメート結合を介し
てアルコキシシラン構造を有する含フッ素化合物である
ことが好ましい。Embedded image (In the formula, Rf represents a perfluoroalkyl group. Z
Represents a fluorine or trifluoromethyl group. a, b, c,
d and e each independently represent 0 or an integer of 1 or more, and a + b + c + d + e is at least 1 or more, and a, b, c, d, e
The order of the recurring units is not limited in the formula. Y represents hydrogen or an alkyl group having 1 to 4 carbon atoms. X represents hydrogen, bromine or iodine. R
1 represents a hydroxyl group or a hydrolyzable substituent. R 2 is
Represents hydrogen or a monovalent hydrocarbon group. l is 0, 1 or 2
Represents m represents 1, 2 or 3. According to the present invention, the organic substance having an alkoxysilane structure via a carbamate bond at a terminal represented by the following formula (III) is used as a material for improving the wiping property of fingerprints and the like as a slipping property and a stain-preventing function. It is preferably a fluorine compound.
【0039】 Rf{(CH2)nOCONH−R1−Si(OR2)3}m・・・式(III ) (式中、Rfは含フッ素オキサアルキル基あるいは含フ
ッ素アルキル基を含む有機基、nは1〜4の整数、R1
は2価の有機基、R2は1価の有機基、mは1〜4の整
数。) 本発明では、有機系物質の成膜された膜の密着には成膜
対象基材の表面が二酸化珪素を主成分とする膜である
と、滑り性機能、撥水性機能、汚れ防止機能を発揮する
のに密着およびその耐久性の面で好都合である。Rf {(CH 2 ) n OCONH—R 1 —Si (OR 2 ) 3 } m Formula (III) (wherein, Rf is an organic group containing a fluorine-containing oxaalkyl group or a fluorine-containing alkyl group) , N is an integer of 1 to 4, R 1
Is a divalent organic group, R 2 is a monovalent organic group, and m is an integer of 1 to 4. In the present invention, when the surface of the substrate to be formed is a film containing silicon dioxide as a main component, the slipping function, the water repellent function, and the dirt prevention function are required for the adhesion of the film formed of the organic substance. It is advantageous in terms of adhesion and its durability to exert.
【0040】さらに、成膜対象基材が反射防止膜付き基
板であると汚れが非常に目立つため、本発明の効果がも
っとも大きく発揮される。すなわち、目標の膜が均一か
つ所望の膜厚が得られてないと、つまり薄すぎれば汚れ
防止機能が不十分であり厚すぎると反射干渉色が大きく
変化したり、表面を擦ったときに白化したりする。Further, when the substrate to be formed is a substrate with an antireflection film, the stain is very conspicuous, and the effect of the present invention is most exerted. That is, if the target film is not uniform and the desired film thickness is not obtained, that is, if the film is too thin, the antifouling function is insufficient. Or
【0041】成膜対象基材が表示画面のフィルター用基
板の用途では、眼精疲労に効果があるので広く普及して
いるが指紋などで表面が汚れることが良く言われている
が、本発明の成膜により得られる膜をを使用すればかか
る課題も解決される。In the use of a filter substrate for a display screen as a substrate on which a film is to be formed, it is widely used because it is effective for asthenopia. However, it is often said that the surface is stained by fingerprints. Such a problem can be solved by using a film obtained by forming a film.
【0042】本発明においては、成膜対象基材が成膜領
域を通過する成膜手法のときその効果が特に大きい。In the present invention, the effect is particularly large when a film forming method is used in which the substrate to be formed passes through the film forming region.
【0043】従来の真空蒸着法の場合、有限量の有機系
物質を蒸着材料とするときは、ベルジャー型の真空蒸着
機、すなわち、蒸着室の下部で蒸発源を加熱し、その上
部に成膜対象基板を固定または回転させる方式をを使用
するのが一般的であるが、この場合は、有限量として入
れる有機系物質の量を決定すればその有機系物質を使い
切ることである程度の膜厚が保証された。しかしなが
ら、図1のような基板通過型成膜であると、通過する基
板長さ分に相当する膜の厚みから換算される、蒸発とし
ての必要量を、有限量として有機系物質として入れる形
となるが、目的とする基板の通過長さに達する前に薬品
切れを起こしたり、前半部分だけ厚膜化してしまうとい
う問題もしばしばあった。In the case of the conventional vacuum evaporation method, when a finite amount of organic substance is used as an evaporation material, a bell jar type vacuum evaporation machine, that is, an evaporation source is heated in a lower part of the evaporation chamber, and a film is formed on the upper part. It is common to use a method of fixing or rotating the target substrate, but in this case, if the amount of the organic substance to be included as a finite amount is determined, a certain film thickness can be obtained by using up the organic substance. Guaranteed. However, in the case of the substrate-passing type film formation as shown in FIG. 1, a necessary amount for evaporation, which is converted from the film thickness corresponding to the length of the substrate to be passed, is included as a finite amount as an organic substance. However, there are often problems that the chemical runs out before reaching the target passage length of the substrate or that the thickness of only the first half is increased.
【0044】これに対し、本発明を適用すれば、通過基
板上に成膜される膜厚も目標とする通過基板長さも必要
十分に成膜可能となる。On the other hand, when the present invention is applied, both the film thickness formed on the passing substrate and the target passing substrate length can be formed sufficiently and sufficiently.
【0045】また、本発明において、有機系物質からな
る膜の膜厚を精度良く所望厚さにコントロールするため
には、その通過速度が実質的に一定速であることが好ま
しい。In the present invention, in order to accurately control the thickness of the film made of an organic substance to a desired thickness, it is preferable that the passing speed is substantially constant.
【0046】特に成膜室が、成膜領域の前後に、成膜対
象基板を多段に収納可能な第1及び第2のストッカーを
有しており、密閉された減圧下で第1のストッカーから
順次該成膜対象基板を取り出し、順次成膜領域を通過さ
せ、順次第2のストッカーに取り入れる薄膜つき基板の
製造方法である場合に好ましく適用される。In particular, the film forming chamber has first and second stockers which can store a substrate to be formed in multiple stages before and after the film forming region. The method is preferably applied to a method of manufacturing a substrate with a thin film in which the substrate to be film-formed is sequentially taken out, sequentially passed through a film-forming region, and sequentially taken into a second stocker.
【0047】以下、本発明の有機膜の成膜法の一例を図
を用いて説明する。ただし、本発明はこれに限定される
ものではない。Hereinafter, an example of a method for forming an organic film according to the present invention will be described with reference to the drawings. However, the present invention is not limited to this.
【0048】図1は、本発明の有機膜の成膜法に用いる
蒸着装置の一例を示す概略図である。FIG. 1 is a schematic view showing an example of a vapor deposition apparatus used in the method of forming an organic film according to the present invention.
【0049】図1において、真空室1は、基板保持室
2,2’、基板搬送室3、蒸着室4で基本的に構成され
ている。これに密閉機構8、8’が設けられており、図
示しない真空ポンプによる減圧下で密閉される。基板6
は、基板保持機構(以下ストッカー)5あるいは5’に
保持されており搬送ローラ7により1枚ずつ蒸着室の上
部を1枚ずつ搬送され通過し成膜され、ストッカー5’
あるいは5に保持されるしくみになっている。有機系物
質9をあらかじめ導電性物質10に付着させ、保持枠1
1に入れておき、これを蒸着室4の内部に入れておく。
抵抗加熱ボート12に電流を出力し、抵抗加熱ボート1
2の輻射熱で有機系物質9の加熱を行う。蒸着室4の内
部の圧力と加熱された有機系物質9の融点沸点昇華点の
関係で蒸発現象が起こる。蒸発された有機系物質は、一
部解離、分解をともなうが蒸発分子となり飛翔する。飛
翔した蒸発分子が水晶振動子13に到達すると、水晶振
動子13の質量が変化しその固有振動数の変化から膜厚
を同定できる。この膜厚に関し、単位時間あたりの膜厚
すなわち堆積速度を算出し、その測定結果が一定になる
ように演算装置15を用いて出力コントローラ16へ制
御信号をおくる。出力コントローラ16は抵抗加熱ボー
ト12へ電流を出力する。このとき、出力に上限あるい
は(かつ)下限を設定する。このようして、目標の蒸発
量すなわち堆積速度に対して実質的に一定になったのを
確認した後、ストッカー5と搬送ローラ7との連携で蒸
着室4の上部の基板搬送室3の内部で基板6を通過させ
成膜させる。一方のストッカーにはいっていた基板6す
べてが蒸着室4の上部を通過したこと確認して抵抗加熱
ボートへの出力を止める。なお、基板上に成膜された膜
と水晶式膜厚計14の堆積速度の関係は実験により厳密
に求められる。In FIG. 1, the vacuum chamber 1 is basically composed of substrate holding chambers 2 and 2 ′, a substrate transfer chamber 3 and a vapor deposition chamber 4. Sealing mechanisms 8 and 8 ′ are provided in this, and are sealed under reduced pressure by a vacuum pump (not shown). Substrate 6
Are held by a substrate holding mechanism (hereinafter referred to as a stocker) 5 or 5 ′, and are transported one by one through the upper part of the vapor deposition chamber one by one by a transport roller 7 to form a film.
Alternatively, it is held at 5. An organic substance 9 is attached to the conductive substance 10 in advance, and the holding frame 1
1 and put it inside the vapor deposition chamber 4.
A current is output to the resistance heating boat 12 and the resistance heating boat 1
The organic material 9 is heated by the radiant heat of Step 2. An evaporation phenomenon occurs due to the relationship between the pressure inside the evaporation chamber 4 and the melting point boiling point sublimation point of the heated organic substance 9. The vaporized organic substance flies as a vaporized molecule with partial dissociation and decomposition. When the flying molecules reach the crystal unit 13, the mass of the crystal unit 13 changes, and the film thickness can be identified from the change in the natural frequency. With respect to this film thickness, the film thickness per unit time, that is, the deposition rate is calculated, and a control signal is sent to the output controller 16 using the arithmetic unit 15 so that the measurement result becomes constant. The output controller 16 outputs a current to the resistance heating boat 12. At this time, an upper limit or (and) a lower limit is set for the output. In this way, after confirming that the evaporation amount, that is, the deposition rate, is substantially constant with respect to the target evaporation amount, the inside of the substrate transfer chamber 3 above the evaporation chamber 4 is operated in cooperation with the stocker 5 and the transfer roller 7. Through the substrate 6 to form a film. After confirming that all the substrates 6 in one stocker have passed through the upper part of the vapor deposition chamber 4, the output to the resistance heating boat is stopped. The relationship between the film formed on the substrate and the deposition rate of the quartz film thickness gauge 14 can be determined strictly by experiments.
【0050】本発明の有機膜の成膜は、例えば、車の窓
ガラス(フロントガラス、リアウインド、側面ウイン
ド)、オートバイのシールド、ヘルメットのシールド、
鏡、手鏡、繊維、布、衣服(たとえば、スカート、ズボ
ン、カッター、背広など香辛料などがついてもすぐふき
取れる)、革製品(車のハンドル、自転車のハンドル、
ハンドバック、かばん、靴)、マウス(パソコン用)、
コップ、花瓶、持ち運び用ケース、電話の受話器、携帯
電話、印鑑、ドアの取手、ショーウインドウ、切符、各
種チケット、銀行などのカード、時計の前面などの用途
に好適に用いられる。The organic film of the present invention can be formed, for example, on a car window glass (windshield, rear window, side window), motorcycle shield, helmet shield,
Mirrors, hand mirrors, textiles, cloths, clothes (for example, skirts, pants, cutters, suits and other spices that can be wiped off quickly), leather goods (car handles, bicycle handles,
Handbag, bag, shoes), mouse (for PC),
It is suitably used for applications such as cups, vases, carrying cases, telephone receivers, mobile phones, seals, door handles, show windows, tickets, various tickets, cards such as banks, and the front of watches.
【0051】[0051]
【実施例】(実施例1) (1)成膜対象基材(基板)作成 成膜対象基材に、市販のポリメチルメタアクリレート板
(三菱レーヨン(株)製、商標”アクリライト”LN−
084、グレー系色原着約70%透過率、厚さ約2m
m)を使用した。ハードコート用塗料としては、特開昭
59−114501号公報の実施例1に記載の、ビニル
トリエトキシシランを氷酢酸で加水分解したものと、メ
チルトリエトキシシランを氷酢酸で加水分解したものを
混合して用いた。この混合溶解物に硬化剤である酢酸ナ
トリウムを加えて塗料とした。この塗料を、上記成膜対
象基板に浸漬法にて塗布し、90℃で3時間キュアして
約2μmの厚さのハードコートを施した。このハードコ
ートを施した基板に、真空蒸着法でZrO2/SiO2
/TiO2/SiO2の順に金属酸化物を蒸着し、比視
感度反射率で約0.5%の反射防止膜つき基板を得た。
基板サイズは、700mm×1200mm×2mmで、
16枚作成した。EXAMPLES (Example 1) (1) Preparation of base material (substrate) for film formation A commercially available polymethyl methacrylate plate (trade name "Acrylite" LN- manufactured by Mitsubishi Rayon Co., Ltd.) was used as a base material for film formation.
084, about 70% transmittance of gray color original, about 2m thick
m) was used. Examples of the hard coat paint include those obtained by hydrolyzing vinyltriethoxysilane with glacial acetic acid and those obtained by hydrolyzing methyltriethoxysilane with glacial acetic acid described in Example 1 of JP-A-59-114501. Used as a mixture. Sodium acetate as a curing agent was added to the mixed solution to obtain a paint. This coating material was applied to the film formation target substrate by an immersion method, cured at 90 ° C. for 3 hours, and a hard coat having a thickness of about 2 μm was applied. A ZrO2 / SiO2 layer is formed on this hard-coated substrate by vacuum evaporation.
A metal oxide was deposited in the order of / TiO2 / SiO2 to obtain a substrate with an antireflection film having a relative luminous reflectance of about 0.5%.
The substrate size is 700mm × 1200mm × 2mm,
Sixteen sheets were made.
【0052】(2)有機系物質および蒸着材料の作成 スチールウール(日本スチールウール(株)製、#1;
線径約0.035mm)を、外径18mm、高さ7mm
肉厚1mmの上方が開放された銅製の容器に詰めた。こ
の中に、m−キシレンヘキサフルオライドにより3%に
希釈した2−(パーフルオロオクチル)エチルトリアミ
ノシラン10gを注いで上記スチールウールに付着さ
せ、常温で約24時間乾燥させ、蒸着材料とした。(2) Preparation of Organic Substance and Deposition Material Steel wool (manufactured by Nippon Steel Wool Co., Ltd., # 1;
Wire diameter about 0.035mm), outer diameter 18mm, height 7mm
It was packed in a copper container having a wall thickness of 1 mm and having an open top. Into this, 10 g of 2- (perfluorooctyl) ethyltriaminosilane diluted to 3% with m-xylene hexafluoride was poured, attached to the steel wool, and dried at room temperature for about 24 hours to obtain a vapor deposition material.
【0053】(3)防汚膜の作成 モリブデン製の高さ(幅)7mmの厚さ0.5mmの材
料を径22mmの円環状にして、抵抗加熱ボートとし
た。円環状の中心部に上記(2)で得られた蒸着材料を
入れた。このようして図1に示す蒸着装置にセットし、
さらに上記(1)で得られた成膜対象基板16枚をスト
ッカーに投入して、蒸着室4の圧力を1×10-3Paと
した。なお、蒸発源と基板搬送面との距離は1000m
mであり、膜厚モニタは、蒸発源から高さ600mm、
蒸発源からの水平距離500mmに配置した。(3) Preparation of Antifouling Film A molybdenum material having a height (width) of 7 mm and a thickness of 0.5 mm was formed into an annular shape having a diameter of 22 mm to obtain a resistance heating boat. The deposition material obtained in the above (2) was put in the center of the ring. Thus, it is set in the vapor deposition device shown in FIG.
Further, 16 substrates for film formation obtained in the above (1) were put into a stocker, and the pressure in the vapor deposition chamber 4 was set to 1 × 10 −3 Pa. The distance between the evaporation source and the substrate transfer surface is 1000 m.
m, the film thickness monitor is 600 mm high from the evaporation source,
It was arranged at a horizontal distance of 500 mm from the evaporation source.
【0054】まず、抵抗加熱ボートに電流650A投入
し、有機系物質を加熱し蒸発させた。膜厚モニタで堆積
速度を測定した。徐々にレイトが上昇し始めた。目標レ
イトは、6オングストローム/sに設定した。膜厚計の
信号をもとにPIDコントロールで抵抗加熱ボートへ出
力する電流値を制御した。レイトが目標の6オングスト
ローム/sよりも下回ったときは電流を上昇させる方向
で、反対に上回ったときは電流を下降させる方向で制御
を行い、出力の電流値に上限として680A、下限とし
て400Aを設定した。電流値は400A〜680Aの
間で制御していた。6オングストローム/s±10%の
範囲内に20秒間制御できているのを確認して、ストッ
カーの中にある基板を水平方向に5m/分の速度で搬送
させた。16枚の基板が搬送されて蒸着室の上部をすべ
て通過し終わる時間は4分であった。First, a current of 650 A was supplied to the resistance heating boat, and the organic substance was heated and evaporated. The deposition rate was measured with a film thickness monitor. Gradually the rate began to rise. The target rate was set at 6 Å / s. The current value output to the resistance heating boat was controlled by PID control based on the signal of the film thickness meter. When the rate falls below the target of 6 angstroms / s, control is performed in the direction of increasing the current, and when the rate exceeds 6 Å / s, control is performed in the direction of decreasing the current. The current value of the output is 680 A as the upper limit and 400 A as the lower limit. Set. The current value was controlled between 400A and 680A. After confirming that control could be performed within a range of 6 Å / s ± 10% for 20 seconds, the substrate in the stocker was transported horizontally at a speed of 5 m / min. The time when 16 substrates were conveyed and completely passed over the upper part of the vapor deposition chamber was 4 minutes.
【0055】この防汚膜作成を上記と全く同じ方法で3
6回実施した。36回とも蒸着室の上部を成膜対象基板
が搬送中、膜厚モニタ上での堆積速度として6オングス
トローム/s±20%の範囲で制御可能であった。The antifouling film was prepared in the same manner as described above.
The test was performed six times. The deposition rate on the film thickness monitor could be controlled within the range of 6 Å / s ± 20% while the substrate to be film-formed was transported over the upper part of the vapor deposition chamber for all 36 times.
【0056】(4)防汚膜の評価 (1)膜厚 16枚の基板についた防汚膜の膜厚を搬送方向に16点
(1点/1枚)とり、超薄切片法によるサンプル作成で
透過型電子顕微鏡(日立製H−600型)で40000
0倍の写真で測定した。その結果、16点とも4nmから
8nmの膜厚になっていた。(4) Evaluation of Antifouling Film (1) Film Thickness The film thickness of the antifouling film on 16 substrates was set at 16 points (1 point / 1 sheet) in the transport direction, and a sample was prepared by an ultra-thin section method. 40000 with transmission electron microscope (H-600 manufactured by Hitachi)
It was measured on a photograph of 0 times. As a result, the thickness of all 16 points was from 4 nm to 8 nm.
【0057】(2)撥水性 16枚の基板を16点(1点/1枚)とり接触角計(協
和界面科学(株)製、CA−D型)を使用して、室温で
直径1.5mmの水滴を針先に作り、これをサンプル表
面に接触させて液滴をつくった。このときに生ずる液滴
と面との角度を測定し、静止接触角とした。16点とも
110゜から111゜であった。(2) Water repellency Sixteen substrates were taken at 16 points (1 point / 1 sheet), and a contact angle meter (manufactured by Kyowa Interface Science Co., Ltd., CA-D type) was used. A 5 mm water droplet was formed at the tip of the needle, and this was brought into contact with the sample surface to form a droplet. The angle between the liquid droplet and the surface generated at this time was measured and defined as a static contact angle. All 16 points ranged from 110 ° to 111 °.
【0058】(3)反射干渉色 反射防止膜による反射干渉色が淡い青紫系の色であった
が、防汚膜成膜前後でほとんど変化が見られなかった。(3) Reflection interference color The reflection interference color by the antireflection film was a pale bluish purple color, but hardly changed before and after the formation of the antifouling film.
【0059】(4)外観 透過色を確認したところ、防汚膜成膜前後で変化が見ら
れなかった。もちろん白化などの問題もなかった。(4) Appearance When the transmitted color was confirmed, no change was observed before and after the formation of the antifouling film. Of course, there was no problem such as whitening.
【0060】(5)拭き汚れ 東レ(株)製のめがね拭き(商標"トレシー")で何回も
擦ったが、拭き汚れは発生しなかった。(5) Wiping stains The glass was wiped many times with a glass wiper (trade name "Toraysee") manufactured by Toray Industries, Ltd., but no wiping stains were generated.
【0061】(6)耐久性 東レ(株)のめがね拭き(商標"トレシー")にエタノー
ルをしみこませ2kg/cm2の圧力で100回擦過し
た。接触角の変化を測定したが、変化は2゜以下であっ
た。(6) Durability Ethanol was impregnated into a glass wipe (trade name “Toraysee”) manufactured by Toray Industries, Inc. and rubbed 100 times at a pressure of 2 kg / cm 2 . The change in the contact angle was measured, and the change was 2 ° or less.
【0062】(7)指紋のふき取り性 鼻の油をつけ、東レ(株)製めがね拭き(商標"トレシ
ー")にて拭き取ったところ、5回程の払拭操作で簡単
にその油がふき取れた。(7) Wiping of Fingerprints Nose oil was applied and wiped off with Toray Co., Ltd.'s eyeglass wiping (trade name "Tresea"). The oil was easily wiped off by about 5 wiping operations.
【0063】上記評価を36回実施したが、ほぼ同様な
結果となった。The above evaluation was performed 36 times, and almost the same results were obtained.
【0064】(実施例2) (1)成膜対象基板作成 実施例1と全く同様に作成した。(Example 2) (1) Preparation of substrate for film formation A film was formed in exactly the same manner as in Example 1.
【0065】(2)有機系物質および蒸着材料の作成 スチールウール(日本スチールウール(株)製、#1;
線径約0.035mm)を、外径18mm高さ7mm肉
厚1mmの上方が開放された銅製の容器に詰めた。この
中に、パーフルオロヘキサンで3%に希釈した下式(I
V)(2) Preparation of Organic Substance and Deposition Material Steel wool (manufactured by Nippon Steel Wool Co., Ltd., # 1;
(A wire diameter of about 0.035 mm) was packed in a copper container having an outer diameter of 18 mm, a height of 7 mm, and a thickness of 1 mm and having an open top. In this, the following formula (I) diluted to 3% with perfluorohexane was used.
V)
【0066】[0066]
【化3】 で示される化合物(分子量約5000)10gを上記ス
チールウールに付着させ、常温で約24時間乾燥させ、
蒸着材料とした。Embedded image Is attached to the steel wool and dried at room temperature for about 24 hours.
It was used as an evaporation material.
【0067】(3)防汚膜の作成 モリブデン製の高さ(幅)7mmの厚さ0.5mmの材
料を径22mmの円環状にして、抵抗加熱ボートとし
た。円環状の中心部に上記(2)で得られた蒸着材料を
入れた。このようして図1に示す蒸着装置にセットし、
さらに上記(1)で得られた成膜対象基板16枚をスト
ッカーに投入して、蒸着室4の圧力を1×10-3Paと
した。なお、蒸発源と基板搬送面との距離は1000m
mであり、膜厚モニタは、蒸発源から高さ600mm、
蒸発源からの水平距離500mmに配置した。(3) Preparation of Antifouling Film A material of molybdenum having a height (width) of 7 mm and a thickness of 0.5 mm was formed into an annular shape having a diameter of 22 mm to obtain a resistance heating boat. The deposition material obtained in the above (2) was put in the center of the ring. Thus, it is set in the vapor deposition device shown in FIG.
Further, 16 substrates for film formation obtained in the above (1) were put into a stocker, and the pressure in the vapor deposition chamber 4 was set to 1 × 10 −3 Pa. The distance between the evaporation source and the substrate transfer surface is 1000 m.
m, the film thickness monitor is 600 mm high from the evaporation source,
It was arranged at a horizontal distance of 500 mm from the evaporation source.
【0068】まず、抵抗加熱ボートに電流600A投入
し、有機系物質を加熱し蒸発させた。膜厚モニタで堆積
速度を測定した。徐々にレイトが上昇し始めた。目標レ
イトは、6オングストローム/sに設定した。膜厚計の
信号をもとにPIDコントロールで抵抗加熱ボートへ出
力する電流値を制御した。レイトが目標の6オングスト
ローム/sよりも下回ったときは電流を上昇させる方向
で、反対に上回ったときは電流を下降させる方向で制御
を行い、出力の電流値に上限として620A、下限とし
て450Aを設定した。電流値は450A〜620Aの
間で制御していた。6オングストローム/s±10%の
範囲内に20秒間制御できているのを確認して、ストッ
カーの中にある基板を水平方向に5m/分の速度で搬送
させた。16枚の基板が搬送されて蒸着室の上部をすべ
て通過し終わる時間は4分であった。First, an electric current of 600 A was applied to the resistance heating boat to heat and evaporate the organic substance. The deposition rate was measured with a film thickness monitor. Gradually the rate began to rise. The target rate was set at 6 Å / s. The current value output to the resistance heating boat was controlled by PID control based on the signal of the film thickness meter. When the rate falls below the target of 6 Å / s, control is performed in the direction of increasing the current, and when the rate exceeds the target, the direction of decreasing the current is controlled. The upper limit of the output current value is 620 A and the lower limit is 450 A. Set. The current value was controlled between 450A and 620A. After confirming that control could be performed within a range of 6 Å / s ± 10% for 20 seconds, the substrate in the stocker was transported horizontally at a speed of 5 m / min. The time when 16 substrates were conveyed and completely passed over the upper part of the vapor deposition chamber was 4 minutes.
【0069】この防汚膜作成を上記と全く同じ方法で2
4回実施した。24回とも蒸着室の上部を成膜対象基板
が搬送中、膜厚モニタ上での堆積速度として6オングス
トローム/s±20%の範囲で制御可能であった。The antifouling film was prepared in exactly the same manner as described above.
The test was performed four times. In all cases, the deposition rate on the film thickness monitor could be controlled within the range of 6 Å / s ± 20% while the substrate to be film-formed was being transported above the vapor deposition chamber 24 times.
【0070】(4)防汚膜の評価 (1)膜厚 16枚の基板についた防汚膜の膜厚を搬送方向に16点
(1点/1枚)とり、超薄切片法によるサンプル作成で
透過型電子顕微鏡(日立製H−600型)で40000
0倍の写真で測定した。その結果、16点とも4nmから
8nmの膜厚になっていた。(4) Evaluation of Antifouling Film (1) Film Thickness The film thickness of the antifouling film on 16 substrates was set at 16 points (1 point / 1 sheet) in the transport direction, and a sample was prepared by an ultra-thin section method. 40000 with transmission electron microscope (H-600 manufactured by Hitachi)
It was measured on a photograph of 0 times. As a result, the thickness of all 16 points was from 4 nm to 8 nm.
【0071】(2)撥水性 16枚の基板を16点(1点/1枚)とり接触角計(協
和界面科学(株)製、CA−D型)を使用して、室温で
直径1.5mmの水滴を針先に作り、これをサンプル表
面に接触させて液滴を作った。このときに生ずる液滴と
面との角度を測定し、静止接触角とした。16点とも1
10゜から111゜であった。(2) Water repellency 16 substrates (16 points (1 point / 1 sheet)) were taken and a contact angle meter (manufactured by Kyowa Interface Science Co., Ltd., CA-D type) was used. A 5 mm water droplet was formed at the tip of the needle, and this was brought into contact with the sample surface to form a droplet. The angle between the liquid droplet and the surface generated at this time was measured and defined as a static contact angle. All 16 points are 1
It was between 10 ° and 111 °.
【0072】(3)反射干渉色 反射防止膜による反射干渉色が淡い青紫系の色であった
が、防汚膜成膜前後でほとんど変化が見られなかった。(3) Reflection interference color The reflection interference color by the antireflection film was a pale bluish purple color, but hardly changed before and after the formation of the antifouling film.
【0073】(4)外観 透過色を確認したところ、防汚膜成膜前後で変化が見ら
れなかった。もちろん白化などの問題もなかった。(4) Appearance When the transmitted color was confirmed, no change was observed before and after the formation of the antifouling film. Of course, there was no problem such as whitening.
【0074】(5)拭き汚れ 東レ(株)製のめがね拭き(商標"トレシー")で何回も
擦ったが拭き汚れは発生しなかった。(5) Wiping dirt The glass was wiped many times with Toray Co., Ltd. (trade name "Toraysee"), but no wiping dirt was generated.
【0075】(6)耐久性 東レ(株)のめがね拭き(商標"トレシー")にエタノー
ルをしみこませ2kg/cm2の圧力で100回擦過し
た。接触角の変化を測定したが、変化は2゜以下であっ
た。(6) Durability Ethanol was impregnated into a glass wipe (trade name “Toraysee”) manufactured by Toray Industries, Inc. and rubbed 100 times at a pressure of 2 kg / cm 2 . The change in the contact angle was measured, and the change was 2 ° or less.
【0076】(7)指紋のふき取り性 鼻の油をつけ、東レ(株)製めがね拭き(商標"トレシ
ー")にて拭き取ったところ、3回程の払拭操作で簡単
にその油がふき取れた。(7) Wipeability of Fingerprint The nose oil was applied and wiped off with Toray Co., Ltd. eyeglass wiping (trademark "Tresea"). The oil was easily wiped off by three wiping operations.
【0077】上記評価を24回実施したが、ほぼ同様な
結果となった。The above evaluation was performed 24 times, and almost the same results were obtained.
【0078】(実施例3) (1)成膜対象基板作成 実施例1と全く同様に作成した。 (2)有機系物質および蒸着材料の作成 スチールウール(日本スチールウール(株)製、#1;
線径約0.035mm)を、外径18mm高さ7mm肉
厚1mmの上方が開放された銅製の容器に詰めた。この
中に、下記合成例に示す液体1gを上記スチールウール
に付着させ、常温で約24時間乾燥させ、蒸着材料とし
た。 (合成例)HO-CH2CF2(CF2CF2O)n-CF2CH2-OH(パーフル
オロポリエチレングリコール系化合物 数平均分子量1
500)15mmolと50度窒素雰囲気下でイソシア
ナートプロピロトリエトキシシラン(OCN-CH2CH2CH2-Si
(OCH2CH3)3)30mmolとDBTDL(ジブチル錫ジラウ
レート:触媒)0.01gを、ジエチルエーテル20g
中に溶解し滴下した後、8時間環流攪拌、反応させた
後、溶媒を留去したところ白色の粘性の液体が得られ
た。(Example 3) (1) Preparation of substrate for film formation A substrate was formed in exactly the same manner as in Example 1. (2) Preparation of organic substances and evaporation materials Steel wool (manufactured by Nippon Steel Wool Co., Ltd., # 1;
(A wire diameter of about 0.035 mm) was packed in a copper container having an outer diameter of 18 mm, a height of 7 mm, and a thickness of 1 mm and having an open top. 1 g of the liquid shown in the following synthesis example was adhered to the steel wool and dried at room temperature for about 24 hours to obtain a vapor deposition material. (Synthesis example) HO-CH 2 CF 2 (CF 2 CF 2 O) n-CF 2 CH 2 —OH (Perfluoropolyethylene glycol-based compound Number average molecular weight 1
500) Isocyanate propyl pyrotriethoxysilane (OCN-CH 2 CH 2 CH 2 -Si
(OCH 2 CH 3 ) 3 ) 30 mmol and 0.01 g of DBTDL (dibutyltin dilaurate: catalyst) were added to 20 g of diethyl ether.
After dissolving and dropping in the mixture, the mixture was refluxed and stirred for 8 hours, and reacted, and then the solvent was distilled off to obtain a white viscous liquid.
【0079】(3)防汚膜の作成 モリブデン製の高さ(幅)7mmの厚さ0.5mmの材
料を、径22mmの円環状にして、抵抗加熱ボートとし
た。円環状の中心部に上記(2)で得られた蒸着材料を
入れた。このようして図1に示す蒸着装置にセットし、
さらに上記(1)で得られた成膜対象基板16枚をスト
ッカーに投入して、蒸着室4の圧力を1×10-3Paと
した。なお、蒸発源と基板搬送面との距離は1000m
mであり、膜厚モニタは、蒸発源から高さ600mm、
蒸発源からの水平距離500mmに配置した。(3) Preparation of Antifouling Film A molybdenum material having a height (width) of 7 mm and a thickness of 0.5 mm was formed into an annular shape having a diameter of 22 mm to obtain a resistance heating boat. The deposition material obtained in the above (2) was put in the center of the ring. Thus, it is set in the vapor deposition device shown in FIG.
Further, 16 substrates for film formation obtained in the above (1) were put into a stocker, and the pressure in the vapor deposition chamber 4 was set to 1 × 10 −3 Pa. The distance between the evaporation source and the substrate transfer surface is 1000 m.
m, the film thickness monitor is 600 mm high from the evaporation source,
It was arranged at a horizontal distance of 500 mm from the evaporation source.
【0080】まず、抵抗加熱ボートに電流600A投入
し、有機系物質を加熱し蒸発させた。膜厚モニタで堆積
速度を測定した。徐々にレイトが上昇し始めた。目標レ
イトは、6オングストローム/sに設定した。膜厚計の
信号をもとにPIDコントロールで抵抗加熱ボートへ出
力する電流値を制御した。レイトが目標の6オングスト
ローム/sよりも下回ったときは電流を上昇させる方向
で、反対に上回ったときは電流を下降させる方向で制御
を行い、出力の電流値に上限として600A、下限とし
て200Aを設定した。電流値は200A〜600Aの
間で制御していた。6オングストローム/s±10%の
範囲内に20秒間制御できているのを確認して、ストッ
カーの中にある基板を水平方向に5m/分の速度で搬送
させた。16枚の基板が搬送されて蒸着室の上部をすべ
て通過し終わる時間は4分であった。First, an electric current of 600 A was applied to the resistance heating boat to heat and evaporate the organic substance. The deposition rate was measured with a film thickness monitor. Gradually the rate began to rise. The target rate was set at 6 Å / s. The current value output to the resistance heating boat was controlled by PID control based on the signal of the film thickness meter. When the rate falls below the target of 6 angstroms / s, control is performed in the direction of increasing the current, and when the rate exceeds the target, the current is decreased. The upper limit of the output current value is 600 A and the lower limit is 200 A. Set. The current value was controlled between 200A and 600A. After confirming that control could be performed within a range of 6 Å / s ± 10% for 20 seconds, the substrate in the stocker was transported horizontally at a speed of 5 m / min. The time when 16 substrates were conveyed and completely passed over the upper part of the vapor deposition chamber was 4 minutes.
【0081】この防汚膜作成を上記と全く同じ方法で3
6回実施した。36回とも蒸着室の上部を成膜対象基板
が搬送中、膜厚モニタ上での堆積速度として6オングス
トローム/s±20%の範囲で制御可能であった。The antifouling film was prepared in the same manner as described above.
The test was performed six times. The deposition rate on the film thickness monitor could be controlled within the range of 6 Å / s ± 20% while the substrate to be film-formed was transported over the upper part of the vapor deposition chamber for all 36 times.
【0082】(4)防汚膜の評価 (1)膜厚 16枚の基板についた防汚膜の膜厚を搬送方向に16点
(1点/1枚)とり超薄切片法によるサンプル作成で透
過型電子顕微鏡(日立製H−600型)で400000
倍の写真で測定した。その結果、16点とも4nmから8
nmの膜厚になっていた。(4) Evaluation of Antifouling Film (1) Film Thickness The film thickness of the antifouling film on 16 substrates was set at 16 points (1 point / 1 sheet) in the transport direction, and a sample was prepared by an ultra-thin section method. 400,000 with a transmission electron microscope (H-600 manufactured by Hitachi)
Measurements were taken at × magnification. As a result, all 16 points were from 4 nm to 8
It had a thickness of nm.
【0083】(2)撥水性 16枚の基板を16点(1点/1枚)とり接触角計(協
和界面科学(株)製、CA−D型)を使用して、室温で
直径1.5mmの水滴を針先に作り、これをサンプル表
面に接触させて液滴をつくった。この時に生ずる液滴と
面との角度を測定し、静止接触角とした。16点とも1
10゜から111゜であった。(2) Water repellency 16 substrates (16 points (1 point / 1 sheet)) were taken and a contact angle meter (type CA-D, manufactured by Kyowa Interface Science Co., Ltd.) was used. A 5 mm water droplet was formed at the tip of the needle, and this was brought into contact with the sample surface to form a droplet. The angle between the droplet and the surface generated at this time was measured and defined as the static contact angle. All 16 points are 1
It was between 10 ° and 111 °.
【0084】(3)反射干渉色 反射防止膜による反射干渉色が淡い青紫系の色であった
が、防汚膜成膜前後でほとんど変化が見られなかった。(3) Reflection interference color The reflection interference color by the antireflection film was a pale blue-violet color, but almost no change was observed before and after the formation of the antifouling film.
【0085】(4)外観 透過色を確認したところ、防汚膜成膜前後で変化が見ら
れなかった。もちろん白化などの問題もなかった。(4) Appearance When the transmitted color was confirmed, no change was observed before and after the formation of the antifouling film. Of course, there was no problem such as whitening.
【0086】(5)拭き汚れ 東レ(株)製のめがね拭き(商標"トレシー")で何回も
擦ったが拭き汚れは発生しなかった。(5) Wiping dirt The glass was wiped many times with Toray Co., Ltd.'s eyeglass wiping (trade name "Toraysee"), but no wiping dirt was generated.
【0087】(6)耐久性 東レ(株)のめがね拭き(商標"トレシー")にエタノー
ルをしみこませ2kg/cm2の圧力で100回擦過し
た。接触角の変化を測定したが、変化は2゜以下であっ
た。(6) Durability Ethanol was soaked in a glass wipe (trade name “Toraysee”) manufactured by Toray Industries, Inc. and rubbed 100 times at a pressure of 2 kg / cm 2 . The change in the contact angle was measured, and the change was 2 ° or less.
【0088】(7)指紋のふき取り性 鼻の油をつけ、東レ(株)製めがね拭き(商標"トレシ
ー")にて拭き取ったところ、1回程の払拭操作で簡単
にその油がふき取れた。(7) Wiping ability of fingerprints The oil of the nose was applied and wiped off with a glass wiper (trade name "Toraysee", manufactured by Toray Industries, Inc.). The oil was easily wiped off by a single wiping operation.
【0089】上記評価を36回実施したが、ほぼ同様な
結果となった。The above evaluation was performed 36 times, and almost the same results were obtained.
【0090】(実施例4) (1)成膜対象基板作成 実施例1と全く同様に作成した。(Example 4) (1) Preparation of substrate for film formation A substrate was formed in exactly the same manner as in Example 1.
【0091】(2)有機系物質および蒸着材料の作成 外径18mm高さ7mm肉厚1mmの上方が開放された
銅製の容器に、下記合成例に示す液体を1gを液体のま
ま入れ、蒸着材料とした。(2) Preparation of Organic Substance and Vapor Deposition Material In a copper container having an outer diameter of 18 mm, a height of 7 mm, and a thickness of 1 mm and an open upper side, 1 g of the liquid shown in the following synthesis example was left as it was. And
【0092】(合成例)HO-CH2CF2(CF2CF2O)n-CF2CH2-O
H(パーフルオロポリエチレングリコール系化合物 数
平均分子量1500)15mmolと50度窒素雰囲気
下でイソシアナートプロピロトリエトキシシラン(OCN-
CH2CH2CH2-Si(OCH2CH3)3)30mmolとDBTDL(ジブ
チル錫ジラウレート:触媒)0.01gをジエチルエー
テル20g中に溶解し滴下した後、8時間環流攪拌、反
応させた後、溶媒を留去したところ白色の粘性の液体が
得られた。(Synthesis example) HO-CH 2 CF 2 (CF 2 CF 2 O) n-CF 2 CH 2 -O
H (perfluoropolyethylene glycol-based compound, number average molecular weight 1500) and isocyanate propyl pyrotriethoxysilane (OCN-
After 30 mmol of CH 2 CH 2 CH 2 —Si (OCH 2 CH 3 ) 3 ) and 0.01 g of DBTDL (dibutyltin dilaurate: catalyst) are dissolved in 20 g of diethyl ether and added dropwise, the mixture is refluxed with stirring for 8 hours, and reacted. When the solvent was distilled off, a white viscous liquid was obtained.
【0093】(3)防汚膜の作成 モリブデン製の高さ(幅)7mmの厚さ0.5mmの材
料を径22mmの円環状にして、抵抗加熱ボートとし
た。円環状の中心部に上記(2)で得られた蒸着材料を
入れた。このようして図1に示す蒸着装置にセットし、
さらに上記(1)で得られた成膜対象基板16枚をスト
ッカーに投入して、蒸着室4の圧力を1×10-3Paと
した。なお、蒸発源と基板搬送面との距離は1000m
mであり、膜厚モニタは、蒸発源から高さ600mm、
蒸発源からの水平距離500mmに配置した。(3) Preparation of Antifouling Film A material of molybdenum having a height (width) of 7 mm and a thickness of 0.5 mm was formed into an annular shape having a diameter of 22 mm to obtain a resistance heating boat. The deposition material obtained in the above (2) was put in the center of the ring. Thus, it is set in the vapor deposition device shown in FIG.
Further, 16 substrates for film formation obtained in the above (1) were put into a stocker, and the pressure in the vapor deposition chamber 4 was set to 1 × 10 −3 Pa. The distance between the evaporation source and the substrate transfer surface is 1000 m.
m, the film thickness monitor is 600 mm high from the evaporation source,
It was arranged at a horizontal distance of 500 mm from the evaporation source.
【0094】まず、抵抗加熱ボートに電流600A投入
し、有機系物質を加熱し蒸発させた。膜厚モニタで堆積
速度を測定した。急激にレイトが上昇し始めた。目標堆
積速度は、6オングストローム/sに設定し、2オング
ストローム/sに達した時点で抵抗加熱ボートへの電流
値コントロールを始めた。膜厚計の信号をもとにPID
コントロールで抵抗加熱ボートへ出力する電流値を制御
するのに加えて出力電流値に上下限を設けた。電流値の
上限は500A、下限は450Aに設定した。電流値
は、450A〜500Aの間で制御していた。蒸発レイ
トが6オングストローム/sになった時点で、ストッカ
ーの中にある基板を水平方向に5m/分の速度で搬送さ
せた。16枚の基板が搬送されて蒸着室の上部を通過し
終わる時間は4分であった。材料が突沸する現象は若干
観測されたものの2オングストローム/s〜40オング
ストローム/sの間で制御可能であった。First, a current of 600 A was applied to the resistance heating boat to heat and evaporate the organic substance. The deposition rate was measured with a film thickness monitor. The rate began to rise sharply. The target deposition rate was set to 6 angstroms / s, and when it reached 2 angstroms / s, the current value control to the resistance heating boat was started. PID based on signal from film thickness meter
In addition to controlling the current value output to the resistance heating boat with the control, upper and lower limits are set for the output current value. The upper limit of the current value was set to 500A, and the lower limit was set to 450A. The current value was controlled between 450A and 500A. When the evaporation rate reached 6 Å / s, the substrate in the stocker was transported horizontally at a speed of 5 m / min. The time when the 16 substrates were conveyed and passed through the upper part of the vapor deposition chamber was 4 minutes. Although the phenomenon of bumping of the material was slightly observed, it could be controlled between 2 angstroms / s and 40 angstroms / s.
【0095】(4)防汚膜の評価 (1)膜厚 16枚の基板についた防汚膜の膜厚を搬送方向に16点
(1点/1枚)とり、超薄切片法によるサンプル作成で
透過型電子顕微鏡(日立製H−600型)で40000
0倍の写真で測定した。その結果、16点とも2nmから
35nmの膜厚になっていた。(4) Evaluation of Antifouling Film (1) Film Thickness The film thickness of the antifouling film on 16 substrates was taken at 16 points (1 point / 1 sheet) in the transport direction, and a sample was prepared by an ultra-thin section method. 40000 with transmission electron microscope (H-600 manufactured by Hitachi)
It was measured on a photograph of 0 times. As a result, the thickness of all 16 points was from 2 nm to 35 nm.
【0096】(2)撥水性 16枚の基板を16点(1点/1枚)とり接触角計(協
和界面科学(株)製、CA−D型)を使用して、室温で
直径1.5mmの水滴を針先に作り、これをサンプル表
面に接触させて液滴をつくった。この時に生ずる液滴と
面との角度を測定し、静止接触角とした。16点とも1
08゜から111゜であった。(2) Water repellency Sixteen substrates were taken at 16 points (1 point / 1 sheet), and a contact angle meter (CA-D type, manufactured by Kyowa Interface Science Co., Ltd.) was used. A 5 mm water droplet was formed at the tip of the needle, and this was brought into contact with the sample surface to form a droplet. The angle between the droplet and the surface generated at this time was measured and defined as the static contact angle. All 16 points are 1
It was between 08 ° and 111 °.
【0097】(3)反射干渉色 反射防止膜による反射干渉色が淡い青紫系の色であった
が、防汚膜成膜前後でほとんど変化が見られなかった。(3) Reflection interference color The reflection interference color by the antireflection film was a pale bluish purple color, but hardly changed before and after the formation of the antifouling film.
【0098】(4)外観 透過色を確認したところ、防汚膜成膜前後で変化が見ら
れなかった。もちろん白化などの問題もなかった。(4) Appearance When the transmitted color was confirmed, no change was observed before and after the formation of the antifouling film. Of course, there was no problem such as whitening.
【0099】(5)拭き汚れ 東レ(株)製のめがね拭き(商標"トレシー")で何回も
擦ったが拭き汚れは発生しなかった。(5) Wiping dirt The glass was wiped many times with Toray Co., Ltd. (trade name "Toraysee"), but no wiping dirt was generated.
【0100】(6)耐久性 東レ(株)のめがね拭き(商標"トレシー")にエタノー
ルをしみこませ2kg/cm2の圧力で100回擦過し
た。接触角の変化を測定したが、変化は2゜以下であっ
た。(6) Durability Ethanol was impregnated into a glass wipe (trade name “Toraysee”) manufactured by Toray Industries, Inc., and rubbed 100 times at a pressure of 2 kg / cm 2 . The change in the contact angle was measured, and the change was 2 ° or less.
【0101】(7)指紋のふき取り性 鼻の油をつけ、東レ(株)製めがね拭き(商標"トレシ
ー")にて拭き取ったところ、1回程の払拭操作で簡単
にその油がふき取れた。(7) Wipeability of Fingerprint The oil of the nose was applied and wiped off with a glass wiper (trade name “Toraysee”, manufactured by Toray Industries, Inc.). The oil was easily wiped off by a single wiping operation.
【0102】(比較例1) (1)成膜対象基板作成 実施例1と全く同様に作成した。(Comparative Example 1) (1) Preparation of a substrate to be formed A film was prepared in exactly the same manner as in Example 1.
【0103】(2)有機系物質および蒸着材料の作成 スチールウール(日本スチールウール(株)製、#1;
線径約0.035mm)を、外径18mm高さ7mm肉
厚1mmの上方が開放された銅製の容器に詰めた。この
中に、m−キシレンヘキサフルオライドで3%に希釈し
た2−(パーフルオロオクチル)エチルトリアミノシラ
ン10gを注いで上記スチールウールに付着させ、常温
で約24時間乾燥させ、蒸着材料とした。(2) Preparation of Organic Substance and Deposition Material Steel wool (manufactured by Nippon Steel Wool Co., Ltd., # 1;
(A wire diameter of about 0.035 mm) was packed in a copper container having an outer diameter of 18 mm, a height of 7 mm, and a thickness of 1 mm and having an open top. Into this, 10 g of 2- (perfluorooctyl) ethyltriaminosilane diluted to 3% with m-xylene hexafluoride was poured, attached to the steel wool, and dried at room temperature for about 24 hours to obtain a vapor deposition material.
【0104】(3)防汚膜の作成 モリブデン製の高さ(幅)7mmの厚さ0.5mmの材
料を径22mmの円環状にして、抵抗加熱ボートとし
た。円環状の中心部に上記(2)で得られた蒸着材料を
入れた。このようして水晶モニタとそれに基づく蒸発源
コントロールシステムを持たない図1に示す蒸着装置に
セットし、さらに上記(1)で得られた成膜対象基板1
6枚をストッカーに投入して、蒸着室4の圧力を1×1
0-3Paとした。なお、蒸発源と基板搬送面との距離は
1000mmであり、膜厚モニタを、蒸発源から高さ6
00mm、蒸発源からの水平距離500mmに配置し
た。(3) Preparation of antifouling film A molybdenum material having a height (width) of 7 mm and a thickness of 0.5 mm was formed into an annular shape having a diameter of 22 mm to obtain a resistance heating boat. The deposition material obtained in the above (2) was put in the center of the ring. In this manner, the substrate 1 is set in the vapor deposition apparatus shown in FIG. 1 which does not have the crystal monitor and the evaporation source control system based on the crystal monitor.
Six sheets are put into a stocker, and the pressure of the vapor deposition chamber 4 is set to 1 × 1
0 -3 Pa. The distance between the evaporation source and the substrate transfer surface is 1000 mm, and the film thickness monitor is set at a height of 6 mm from the evaporation source.
00 mm and a horizontal distance of 500 mm from the evaporation source.
【0105】まず、抵抗加熱ボートに電流650A投入
し、有機系物質を加熱し蒸発させた。蒸発に伴い、蒸着
室内の圧力は上昇してやがて降下した。圧力が3×10
-3Paに上昇した時点でストッカーの中にある基板を水
平方向に5m/分の速度で搬送させた。その後、徐々に
圧力が上昇し続け、ちょうど6枚目の基板が蒸着室の上
部にきたとき、圧力が2×10-2Paの極大となり、そ
の後圧力が下降し始め16枚目の基板ホルダーが通過し
終わったときには圧力が4×10-3Paとなっていた。
膜厚モニタ上での堆積速度は、成膜対象基板の3枚目が
蒸着室の上部を通過しているとき4オングストローム/
s、5枚目が通過しているとき18オングストローム/
s、6枚目が通過しているとき80オングストローム/
s、7枚目が通過しているとき50オングストローム/
s、8枚目が通過しているとき2オングストローム/s
であった。1枚目〜2枚目、9枚目〜16枚目は2オン
グストローム/s未満であった。First, a current of 650 A was supplied to the resistance heating boat, and the organic substance was heated and evaporated. With the evaporation, the pressure in the deposition chamber rose and eventually fell. Pressure is 3 × 10
When the pressure rose to -3 Pa, the substrate in the stocker was transported horizontally at a speed of 5 m / min. Thereafter, the pressure gradually increases, and when the sixth substrate just reaches the upper part of the vapor deposition chamber, the pressure reaches a local maximum of 2 × 10 -2 Pa, and then the pressure starts to decrease, and the sixteenth substrate holder starts to move. When the passage was completed, the pressure was 4 × 10 −3 Pa.
The deposition rate on the film thickness monitor is 4 angstroms / degree when the third substrate to be deposited passes through the upper part of the deposition chamber.
s when the 5th sheet has passed 18 angstrom /
s, 80 angstroms /
s, 50 angstroms /
s, 2 angstrom / s when the 8th sheet is passing
Met. The first to second sheets and the ninth to sixteenth sheets were less than 2 Å / s.
【0106】(4)防汚膜の評価 (1)膜厚 16枚の基板についた防汚膜の膜厚を搬送方向に16点
(1点/1枚)とり、超薄切片法によるサンプル作成で
透過型電子顕微鏡(日立製H−600型)で40000
0倍の写真で測定した。1〜2枚目は、ほとんど膜厚が
観察されなかった。3枚目が4nm、4枚目が6nm、5枚
目が30nm、6枚目が110nm、7枚目が80nm、の膜
厚になっていた。8枚目が2nm、9枚目以降は膜厚がほ
とんど観察されなかった。(4) Evaluation of Antifouling Film (1) Film Thickness The film thickness of the antifouling film on 16 substrates was set at 16 points (1 point / 1 sheet) in the transport direction, and a sample was prepared by an ultra-thin section method. 40000 with transmission electron microscope (H-600 manufactured by Hitachi)
It was measured on a photograph of 0 times. In the first and second sheets, almost no film thickness was observed. The third sheet had a thickness of 4 nm, the fourth sheet had a thickness of 6 nm, the fifth sheet had a thickness of 30 nm, the sixth sheet had a thickness of 110 nm, and the seventh sheet had a thickness of 80 nm. The 8th sheet had a thickness of 2 nm, and the ninth and subsequent sheets showed almost no film thickness.
【0107】(2)撥水性 16枚の基板を16点(1点/1枚)とり接触角計(協
和界面科学(株)製、CA−D型)を使用して、室温で
直径1.5mmの水滴を針先に作り、これをサンプル表
面に接触させて液滴をつくった。この時に生ずる液滴と
面との角度を測定し、静止接触角とした。1枚目が30
゜、2枚目が40゜、3、4枚目が110゜、5枚目が
111゜、6枚目が112゜、7枚目が111゜、8枚
目が109゜、9枚目が60゜、10枚目以降は20゜
〜30゜であった。(2) Water repellency 16 substrates (16 points (1 point / 1 sheet)) were taken and a contact angle meter (type CA-D, manufactured by Kyowa Interface Science Co., Ltd.) was used. A 5 mm water droplet was formed at the tip of the needle, and this was brought into contact with the sample surface to form a droplet. The angle between the droplet and the surface generated at this time was measured and defined as the static contact angle. The first one is 30
゜ The second sheet is 40 ゜, the third and fourth sheets are 110 ゜, the fifth sheet is 111 ゜, the sixth sheet is 112 ゜, the seventh sheet is 111 ゜, the eighth sheet is 109 ゜, and the ninth sheet is The angle was 60 ° to 20 ° to 30 ° after the 10th sheet.
【0108】(3)反射干渉色 反射防止膜による反射干渉色が淡い青紫系の色であっ
た。1枚目から4枚目までと8枚目以降は防汚膜成膜前
後でほとんど変化が見られず、5枚目は若干青っぽい色
に変化し、6、7枚目は、非常に大きな色変化で青い反
射干渉色になった。(3) Reflection interference color The reflection interference color by the antireflection film was a pale bluish purple color. From the first sheet to the fourth sheet and after the eighth sheet, little change was observed before and after the formation of the antifouling film, the fifth sheet changed to a slightly bluish color, and the sixth and seventh sheets showed a very large color. The change resulted in a blue reflective interference color.
【0109】(4)外観 透過色を確認したところ、防汚膜成膜前後で変化が見ら
れなかった。6枚目、7枚目のみ若干白化して見えた。(4) Appearance When the transmitted color was confirmed, no change was observed before and after the formation of the antifouling film. Only the sixth and seventh sheets appeared slightly whitened.
【0110】(5)拭き汚れ 6枚目、7枚目は東レ(株)製のめがね拭き(商標"ト
レシー")で何回も擦ったところ、汚れ防止機能膜をつ
けたのにも関わらず、拭けば拭くほど拭いた部分が白化
しが拭き汚れが発生した。5枚目は、うっすら拭き汚れ
傾向があるようにも見えた。(5) Wiping dirt The sixth and seventh sheets were rubbed many times with Toray Co., Ltd.'s eyeglass wiping (trademark "Toraysee"). The more the wiper was wiped, the more the wiped portion was whitened, but wiping stains occurred. The fifth sheet also appeared to have a slight tendency to wipe.
【0111】(6)耐久性 東レ(株)のめがね拭き(商標"トレシー")にエタノー
ルをしみこませ2kg/cm2の圧力で100回擦過し
た。接触角の変化を測定したが、変化は2゜以下であっ
た。(6) Durability Ethanol was impregnated into a glass wipe (trade name “Toraysee”) manufactured by Toray Industries, Inc. and rubbed 100 times at a pressure of 2 kg / cm 2 . The change in the contact angle was measured, and the change was 2 ° or less.
【0112】(7)指紋のふき取り性 鼻の油をつけ、東レ(株)製めがね拭き(商標"トレシ
ー")にて拭き取ったところ、5回程の払拭で簡単にそ
の油がふき取れたのは3、4、5、8枚目の基板のみで
あった。(7) Fingerprint wiping property Nose oil was applied and wiped off with Toray Co., Ltd. eyeglass wiping (trademark "Tresee"). When the wiping was performed about 5 times, the oil was easily wiped off. It was only the third, fourth, fifth and eighth substrates.
【0113】(比較例2)比較例1の結果から、図1に
示す蒸着装置で製造を行う場合は、膜厚モニタ上での堆
積速度が2オングストローム/s〜18オングストロー
ム/sの間の範囲内にあるとき成膜対象基板に成膜され
た防汚膜は良好と判断した。従って該範囲外であるとき
は異常とみなした。(Comparative Example 2) Based on the results of Comparative Example 1, when manufacturing is performed using the vapor deposition apparatus shown in FIG. 1, the deposition rate on the film thickness monitor is in the range of 2 Å / s to 18 Å / s. When it was within, the antifouling film formed on the film formation target substrate was judged to be good. Therefore, when it was out of the range, it was regarded as abnormal.
【0114】抵抗加熱ボートへの出力電流値に上下限を
設定する以外は実施例1と全く同じ方法で実施した。1
00回実施して21回異常が発生した。このうち上限の
18オングストローム/sを超えたものは14回、下限
の2オングストローム/sを下回ったものは7回であっ
た。異常発生率は21%であった。The procedure was performed in exactly the same manner as in Example 1 except that the upper and lower limits were set for the output current value to the resistance heating boat. 1
The operation was performed 00 times and an abnormality occurred 21 times. Of these, 14 times exceeded the upper limit of 18 Å / s, and 7 times exceeded the lower limit of 2 Å / s. The abnormality occurrence rate was 21%.
【0115】[0115]
【発明の効果】本発明によれば、真空蒸着法のようなド
ライプロセスにおいて、有機ポリシロキサン系化合物ま
たはパーフルオロアルキル基含有化合物を含む有限量の
有機系物質を加熱蒸発させて、成膜対象基材の表面に成
膜し、滑り性機能や撥水性機能や汚れ防止機能などを持
たせる場合に、膜厚を制御するとともに、さらに、安定
的に失敗無く、その再現性を実現し、かつその機能を必
要十分に満たす有機膜を製膜することができる。According to the present invention, in a dry process such as a vacuum deposition method, a finite amount of an organic substance containing an organic polysiloxane compound or a perfluoroalkyl group-containing compound is heated and evaporated to form a film-forming object. In the case of forming a film on the surface of the base material and having a slippery function, a water repellent function, a stain prevention function, etc., the film thickness is controlled, and furthermore, the reproducibility is realized stably without failure, and It is possible to form an organic film that satisfies the function as required.
【0116】また、本発明によれば、特に成膜対象基材
の外観を損なうことなく薄い膜を形成することができ
る。また、本発明により得られる有機膜形成基材(基
板)は、各種表示画面の最表面、あるいは各種表示画面
の前面に用いられる光学フィルターの最表面、めがねレ
ンズ等の最表面に用いられ、特に反射防止機能膜に好適
に用いられる。Further, according to the present invention, a thin film can be formed without impairing the appearance of the substrate on which the film is to be formed. Further, the organic film-forming substrate (substrate) obtained by the present invention is used as the outermost surface of various display screens, or the outermost surface of an optical filter used in front of various display screens, or the outermost surface of an eyeglass lens. It is suitably used for an antireflection function film.
【図1】本発明の有機膜の成膜法に用いる蒸着装置の一
例を示す概略図である。FIG. 1 is a schematic view showing an example of a vapor deposition apparatus used for a method for forming an organic film according to the present invention.
1.:真空室 2,2’:基板保持室 3:基板搬送室 4:蒸着室 5,5’:基板保持機構(ストッカー) 6:基板 7:搬送ローラ 8,8’:密閉機構 9:有機系物質 10:導電性物質 11:保持枠 12:抵抗加熱ボート 13:水晶振動子(水晶振動モニタ) 14:膜厚計 15:演算装置 16:出力コントローラー 1. : Vacuum chamber 2, 2 ': Substrate holding chamber 3: Substrate transfer chamber 4: Vapor deposition chamber 5, 5': Substrate holding mechanism (stocker) 6: Substrate 7: Transfer roller 8, 8 ': Sealing mechanism 9: Organic substance 10: Conductive substance 11: Holding frame 12: Resistance heating boat 13: Quartz oscillator (Quartz oscillation monitor) 14: Film thickness gauge 15: Operation device 16: Output controller
───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.7 識別記号 FI テーマコート゛(参考) C09K 3/18 104 C09K 3/18 104 G02B 1/10 C09D 183/08 // C09D 183/08 G02B 1/10 Z Fターム(参考) 2K009 AA07 AA15 BB14 CC03 CC24 CC42 DD02 DD03 EE00 EE05 4D075 BB24Z BB36Z BB92Z CA09 CA34 CA36 DC24 EB16 EB43 4H020 BA36 4J038 DL011 DL031 GA12 GA15 JC35 NA05 NA07 NA09 NA19 PA01 PB09 PC01 4K029 AA09 BA62 BC07 BD09 CA01 DB06 ──────────────────────────────────────────────────続 き Continued on the front page (51) Int.Cl. 7 Identification code FI Theme coat ゛ (Reference) C09K 3/18 104 C09K 3/18 104 G02B 1/10 C09D 183/08 // C09D 183/08 G02B 1 / 10Z F term (reference) 2K009 AA07 AA15 BB14 CC03 CC24 CC42 DD02 DD03 EE00 EE05 4D075 BB24Z BB36Z BB92Z CA09 CA34 CA36 DC24 EB16 EB43 4H020 BA36 4J038 DL011 DL031 GA12 GA15 JC35 NA09 NA09 NA09 NA09 NA09 NA09
Claims (16)
化合物またはパーフルオロアルキル基含有化合物を含む
有機系物質を含む膜を形成する方法において、該有機系
物質を加熱蒸発させ、その蒸発量の測定結果をもとに該
蒸発量を実質的に一定にするように加熱源の出力を制御
するとともに、該出力に上限または/及び下限を設ける
ことを特徴とする有機膜の成膜法。In a method for forming a film containing an organic material containing an organic polysiloxane compound or a perfluoroalkyl group-containing compound on a film-forming target substrate, the organic material is heated and evaporated, and the amount of evaporation is increased. A method for controlling an output of a heating source so as to make the evaporation amount substantially constant based on the measurement result of (1), and providing an upper limit and / or a lower limit to the output.
ことを特徴とする請求項1記載の有機膜の成膜法。2. The method according to claim 1, wherein the heating means of the heating source is a resistance heating method.
あることを特徴とする請求項1または2記載の有機膜の
成膜法。3. The method for forming an organic film according to claim 1, wherein the means for measuring the evaporation amount is a quartz film thickness meter.
nmから30nmになるように制御することを特徴とする請
求項1〜3のいずれかに記載の有機膜の成膜法。4. The film thickness of a film formed on a film forming target substrate is 1
The method for forming an organic film according to claim 1, wherein the thickness is controlled to be from 30 nm to 30 nm.
ることを特徴とする請求項1〜4のいずれかに記載の有
機膜の成膜法。5. The method for forming an organic film according to claim 1, wherein the organic substance is held by a porous material.
されてなることを特徴とする請求項1〜4のいずれかに
記載の有機膜の成膜法。6. The method according to claim 1, wherein the organic substance is attached to a fibrous conductive substance.
ている保持枠に入れることを特徴とする請求項6記載の
有機膜の成膜法。7. The method for forming an organic film according to claim 6, wherein the conductive substance is placed in a holding frame that is open in at least one direction.
特徴とする請求項1〜7のいずれかに記載の有機膜の成
膜法。8. The organic substance, the following formula (I) n-C p F p + 1 CH 2 CH 2 Si (NH 2) 3 ··· (I) ( Here, p is a natural number), a compound represented by The method for forming an organic film according to claim 1, further comprising:
は、フッ素またはトリフルオロメチル基を表す。a,b,c,
d,eは、それぞれ独立して、0または1以上の整数を表
し、a+b+c+d+eは、少なくとも1以上であり、a,b,c,d,e
でくくられた繰り返し単位の存在順序は、式中において
限定されない。Yは、水素又は炭素数1〜4のアルキル
基を表す。Xは、水素、臭素又はヨウ素を表す。R
1は、水酸基又は加水分解可能な置換基を表す。R2は、
水素又は1価の炭化水素基を表す。lは、0、1又は2
を表す。mは、1、2又は3を表す。)で示され、数平
均分子量が500から10000であるケイ素含有有機
フッ素化合物を含むことを特徴とする請求項1〜7のい
ずれかに記載の有機膜の成膜法。9. The organic substance is represented by the following formula (II): (In the formula, Rf represents a perfluoroalkyl group. Z
Represents a fluorine or trifluoromethyl group. a, b, c,
d and e each independently represent 0 or an integer of 1 or more, and a + b + c + d + e is at least 1 or more, and a, b, c, d, e
The order of the recurring units is not limited in the formula. Y represents hydrogen or an alkyl group having 1 to 4 carbon atoms. X represents hydrogen, bromine or iodine. R
1 represents a hydroxyl group or a hydrolyzable substituent. R 2 is
Represents hydrogen or a monovalent hydrocarbon group. l is 0, 1 or 2
Represents m represents 1, 2 or 3. The method according to claim 1, further comprising a silicon-containing organic fluorine compound having a number average molecular weight of 500 to 10,000.
ッ素アルキル基を含む有機基、nは1〜4の整数、R1
は2価の有機基、R2は1価の有機基、mは1〜4の整
数。)で示される末端にカルバメート結合を介してアル
コキシシラン構造を有する含フッ素化合物を含むことを
特徴とする請求項1〜7のいずれかに記載の有機膜の成
膜法。10. The organic substance is represented by the following formula (III): Rf {(CH 2 ) n OC ONH-R 1 —Si (OR 2 ) 3 } m (Formula (III)) An organic group containing a fluorine oxaalkyl group or a fluorine-containing alkyl group, n is an integer of 1 to 4, R 1
Is a divalent organic group, R 2 is a monovalent organic group, and m is an integer of 1 to 4. 8. The method for forming an organic film according to claim 1, further comprising a fluorine-containing compound having an alkoxysilane structure at a terminal represented by a) via a carbamate bond.
成分とする膜で構成されていることを特徴とする請求項
1〜10のいずれかに記載の有機膜の成膜法。11. The method for forming an organic film according to claim 1, wherein the surface of the substrate on which the film is to be formed is made of a film containing silicon dioxide as a main component.
あることを特徴とする請求項1〜11のいずれかに記載
の有機膜の成膜法。12. The method for forming an organic film according to claim 1, wherein the substrate to be formed is a substrate with an antireflection film.
用基材であることを特徴とする請求項1〜11のいずれ
かに記載の有機膜の成膜法。13. The method for forming an organic film according to claim 1, wherein the substrate for film formation is a substrate for a filter of a display screen.
とを特徴とする請求項1記載の有機膜の成膜法。14. The method according to claim 1, wherein the substrate to be formed passes through a film formation region.
を特徴とする請求項1記載の有機膜の成膜法。15. The method according to claim 1, wherein the passing speed is substantially constant.
象基板を多段に収納可能な第1及び第2のストッカーを
有しており、密閉された減圧下で第1のストッカーから
順次該成膜対象基板を取り出し、順次成膜領域を通過さ
せ、順次第2のストッカーに取り入れることを特徴とす
る請求項14または15記載の有機膜の成膜法。16. The film forming chamber has first and second stockers which can store a film formation target substrate in multiple stages before and after the film forming region, and the first stocker is closed under reduced pressure. The method according to claim 14, wherein the substrate to be film-formed is sequentially taken out from the substrate, sequentially passed through a film-forming region, and sequentially taken into a second stocker.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP11139769A JP2000328230A (en) | 1999-05-20 | 1999-05-20 | Method for deposition of organic film |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP11139769A JP2000328230A (en) | 1999-05-20 | 1999-05-20 | Method for deposition of organic film |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JP2000328230A true JP2000328230A (en) | 2000-11-28 |
Family
ID=15252982
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP11139769A Pending JP2000328230A (en) | 1999-05-20 | 1999-05-20 | Method for deposition of organic film |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JP2000328230A (en) |
Cited By (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2001281412A (en) * | 2000-03-31 | 2001-10-10 | Nissha Printing Co Ltd | Antireflection member and method for producing the same |
| FR2826654A1 (en) * | 2001-06-27 | 2003-01-03 | Atofina | COMPOSITION AND PROCESS FOR THE TREATMENT OF SURFACE AND SUBSTRATES LIKELY TO BE SO OBTAINED |
| JP2005187936A (en) * | 2003-12-02 | 2005-07-14 | Seiko Epson Corp | Thin film manufacturing method, optical component manufacturing method, and film forming apparatus |
| WO2009101986A1 (en) * | 2008-02-12 | 2009-08-20 | Fujifilm Corporation | Fluorine-containing polyfunctional silicon compound and method for producing fluorine-containing polyfunctional silicon compound |
| JP2013155408A (en) * | 2012-01-30 | 2013-08-15 | Fujifilm Corp | Method for manufacturing water repellent film and water repellent film manufactured by the manufacturing method |
| JP2017220670A (en) * | 2016-06-02 | 2017-12-14 | ツィンファ ユニバーシティ | Method and apparatus for manufacturing organic thin film transistor |
| JP2018521199A (en) * | 2015-04-16 | 2018-08-02 | セコ カンパニー リミテッド | Antibacterial primer coating agent for vacuum deposition and multiple coating method using the same |
| WO2025263370A1 (en) * | 2024-06-21 | 2025-12-26 | 株式会社ニコン・エシロール | Method for storing vapor deposition source, and method for manufacturing spectacle lens |
-
1999
- 1999-05-20 JP JP11139769A patent/JP2000328230A/en active Pending
Cited By (16)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2001281412A (en) * | 2000-03-31 | 2001-10-10 | Nissha Printing Co Ltd | Antireflection member and method for producing the same |
| JP3457620B2 (en) | 2000-03-31 | 2003-10-20 | 日本写真印刷株式会社 | Anti-reflection member and method of manufacturing the same |
| FR2826654A1 (en) * | 2001-06-27 | 2003-01-03 | Atofina | COMPOSITION AND PROCESS FOR THE TREATMENT OF SURFACE AND SUBSTRATES LIKELY TO BE SO OBTAINED |
| WO2003002572A1 (en) * | 2001-06-27 | 2003-01-09 | E.I. Du Pont De Nemours And Company | Surface treatment composition and method |
| US7276618B2 (en) | 2001-06-27 | 2007-10-02 | E. I. Du Pont De Nemours And Company | Surface treatment composition and process |
| JP2005187936A (en) * | 2003-12-02 | 2005-07-14 | Seiko Epson Corp | Thin film manufacturing method, optical component manufacturing method, and film forming apparatus |
| JP5286289B2 (en) * | 2008-02-12 | 2013-09-11 | 富士フイルム株式会社 | Fluorine-containing polyfunctional silicon compound and method for producing fluorine-containing polyfunctional silicon compound |
| WO2009101986A1 (en) * | 2008-02-12 | 2009-08-20 | Fujifilm Corporation | Fluorine-containing polyfunctional silicon compound and method for producing fluorine-containing polyfunctional silicon compound |
| US8541533B2 (en) | 2008-02-12 | 2013-09-24 | Fujifilm Corporation | Fluorine-containing polyfunctional silicon compound and method for producing fluorine-containing polyfunctional silicon compound |
| CN101945882B (en) * | 2008-02-12 | 2014-09-03 | 富士胶片株式会社 | Fluorine-containing polyfunctional silicon compound and method for producing fluorine-containing polyfunctional silicon compound |
| JP2013155408A (en) * | 2012-01-30 | 2013-08-15 | Fujifilm Corp | Method for manufacturing water repellent film and water repellent film manufactured by the manufacturing method |
| US9012670B2 (en) | 2012-01-30 | 2015-04-21 | Fujifilm Corporation | Method of manufacturing water repellent film and thereby manufactured water repellent film |
| JP2018521199A (en) * | 2015-04-16 | 2018-08-02 | セコ カンパニー リミテッド | Antibacterial primer coating agent for vacuum deposition and multiple coating method using the same |
| JP2017220670A (en) * | 2016-06-02 | 2017-12-14 | ツィンファ ユニバーシティ | Method and apparatus for manufacturing organic thin film transistor |
| US10388896B2 (en) | 2016-06-02 | 2019-08-20 | Tsinghua University | Apparatus and method for forming organic thin film transistor |
| WO2025263370A1 (en) * | 2024-06-21 | 2025-12-26 | 株式会社ニコン・エシロール | Method for storing vapor deposition source, and method for manufacturing spectacle lens |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| EP0548775B1 (en) | Water-repellent metal oxide film coated on glass substrate and method of forming same | |
| US5853800A (en) | Material for and method of preparing water-repellent coatings on optical substrates | |
| US6465108B1 (en) | Process for the production of articles covered with silica-base coats | |
| CN100487071C (en) | Coating film having low refractive index and water repellency | |
| WO2017022638A1 (en) | Glass substrate suitable for cover glass, etc., of mobile display device | |
| JP4887784B2 (en) | Coating with low refractive index and large water contact angle | |
| JP2000328231A (en) | Deposition method by organic material to be deposited by evaporation | |
| JP2000328230A (en) | Method for deposition of organic film | |
| JPH08510089A (en) | Display device including display screen with light absorbing coating | |
| WO2000015428A1 (en) | Functional film and method for preparation thereof, and liquid crystal display element using the same and method for preparation thereof | |
| JP5293180B2 (en) | Coating liquid for coating formation containing phosphoric ester compound and antireflection film | |
| JP2000327997A (en) | Method for forming organic film | |
| JPH11133206A (en) | Anti-reflection filter and character image display device using the anti-reflection filter | |
| JPH01309003A (en) | Antistatic article having water repellency | |
| JPH1026703A (en) | Water-repellent lens | |
| JP2000336334A (en) | Method for producing silica-based membrane-coated article and functional membrane-coated article | |
| JP2001335920A (en) | Vapor deposition source, optical article and the producing method | |
| JPH10133001A (en) | New water-repellent lens | |
| JPH1192177A (en) | Water repellent glass and method for producing the same | |
| JP3579655B2 (en) | Transparent substrate having antifouling hydrophobic coating and method for producing the same | |
| JPH05319867A (en) | Water repellent treatment agent for glass substrate and water repellent treatment method thereof | |
| JP2001183503A (en) | Method of producing optical article | |
| US10830924B2 (en) | Optical article comprising a precursor coating of an anti-fogging coating having anti-fouling properties obtained from an amphiphilic compound | |
| US6833159B1 (en) | Method for applying hydrophobic anti-reflection coatings to lenses and lens blanks | |
| JP3120371B2 (en) | Optical article manufacturing method |