JPS60193530A - Film forming device - Google Patents

Film forming device

Info

Publication number
JPS60193530A
JPS60193530A JP4718284A JP4718284A JPS60193530A JP S60193530 A JPS60193530 A JP S60193530A JP 4718284 A JP4718284 A JP 4718284A JP 4718284 A JP4718284 A JP 4718284A JP S60193530 A JPS60193530 A JP S60193530A
Authority
JP
Japan
Prior art keywords
liquid
cylinder
tank
difference
film
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
Application number
JP4718284A
Other languages
Japanese (ja)
Inventor
Yoshinori Tomita
佳紀 富田
Hiroshi Matsuda
宏 松田
Yukio Nishimura
征生 西村
Yutaka Hirai
裕 平井
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Canon Inc
Original Assignee
Canon Inc
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Canon Inc filed Critical Canon Inc
Priority to JP4718284A priority Critical patent/JPS60193530A/en
Publication of JPS60193530A publication Critical patent/JPS60193530A/en
Pending legal-status Critical Current

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B82NANOTECHNOLOGY
    • B82YSPECIFIC USES OR APPLICATIONS OF NANOSTRUCTURES; MEASUREMENT OR ANALYSIS OF NANOSTRUCTURES; MANUFACTURE OR TREATMENT OF NANOSTRUCTURES
    • B82Y30/00Nanotechnology for materials or surface science, e.g. nanocomposites
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B05SPRAYING OR ATOMISING IN GENERAL; APPLYING FLUENT MATERIALS TO SURFACES, IN GENERAL
    • B05DPROCESSES FOR APPLYING FLUENT MATERIALS TO SURFACES, IN GENERAL
    • B05D1/00Processes for applying liquids or other fluent materials
    • B05D1/18Processes for applying liquids or other fluent materials performed by dipping
    • B05D1/20Processes for applying liquids or other fluent materials performed by dipping substances to be applied floating on a fluid
    • B05D1/202Langmuir Blodgett films (LB films)
    • B05D1/206LB troughs
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B82NANOTECHNOLOGY
    • B82YSPECIFIC USES OR APPLICATIONS OF NANOSTRUCTURES; MEASUREMENT OR ANALYSIS OF NANOSTRUCTURES; MANUFACTURE OR TREATMENT OF NANOSTRUCTURES
    • B82Y40/00Manufacture or treatment of nanostructures

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  • Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Nanotechnology (AREA)
  • Physics & Mathematics (AREA)
  • Condensed Matter Physics & Semiconductors (AREA)
  • General Physics & Mathematics (AREA)
  • Crystallography & Structural Chemistry (AREA)
  • Manufacturing & Machinery (AREA)
  • Composite Materials (AREA)
  • Materials Engineering (AREA)
  • Physical Or Chemical Processes And Apparatus (AREA)
  • Other Surface Treatments For Metallic Materials (AREA)

Abstract

PURPOSE:To improve the accumulation rate of monomolecular films on a solid carrier by providing a liquid tank for spreading molecular groups for forming films and constituting the liquid vessel in such a way that a difference in liquid level arises in the liquid contained in said tank. CONSTITUTION:A liquid tank 1 for spreading molecular groups for forming film is provided and a liquid tank 1 is so constituted that a difference in liquid level arises to the liquid contained in the tank 1. A cylinder 2 is set by utilizing a partition plate 5 consisting of, for example, a rubber blade or the like and after a cylinder 2 is set, liquids 3, 4 are poured into the vessel 1 in such a way that a difference between the high and low liquid levels arises in the respective parts A, B in the liquid vessel 1 segmented by the cylinder 2 and the plate 5. Monomolecular films 11, 12 are thereafter spread on the respective surfaces of the liquids 3, 4 and the cylinder 2 is rotated in an arrow direction, by which the accumulated monomolecular films consisting of the monomolecular films having an improved rate of accumulation and a desired degree of accumulation are obtd. on the cylinder 2. The rotation of the molecules is decreased in the parts A, B according to the above-mentioned constitution and therefore the rate of accumulation is increased.

Description

【発明の詳細な説明】 (1)技術分野 本発明は成膜装置に関する。[Detailed description of the invention] (1) Technical field The present invention relates to a film forming apparatus.

(2)背景技術 従来、液面上に展開された単分子膜を、その支持体であ
る固体担体の表面上に移しとることにより、該担体上に
単分子膜又は単分子累積膜から成る薄膜を成膜する方法
(所謂、ラングミュア・ブロジェット法)が知られてい
るが、この方法に使用される成膜装置は、第1図ないし
第3図に示す垂直浸漬方式、水平付着方式および円筒回
転方式の3つに大別される。
(2) Background Art Conventionally, by transferring a monomolecular film developed on a liquid surface onto the surface of a solid carrier that is its support, a thin film consisting of a monomolecular film or a monomolecular cumulative film is deposited on the support. A method for forming a film (the so-called Langmuir-Blodgett method) is known, but the film forming apparatus used for this method is a vertical immersion method, a horizontal deposition method, and a cylindrical method, as shown in Figures 1 to 3. It is roughly divided into three types of rotation methods.

筑1Mに偏量1.た浜直蛤邊有才の連間装置の其本構成
は、平板状等の所望の形状をした固体担体を、単分子膜
の展開されている液面上を横切るように上下させること
によって、固体担体上に単分子膜又は単分子累積膜を成
膜するものである。この垂直浸漬方式では、固体担体を
上下するための上下装置が比較的構造が簡単にすむとい
う長所がある代りに、単分子膜の固体担体上への累積率
が悪いという問題があった。
Chiku 1M has an uneven amount of 1. The main structure of Tahama Naohamabe Yusai's rengan device is to raise and lower a solid support in a desired shape, such as a flat plate, across the surface of the liquid on which the monomolecular film is being developed. A monomolecular film or a monomolecular cumulative film is formed on a solid support. Although this vertical dipping method has the advantage that the structure of the up-and-down device for raising and lowering the solid carrier is relatively simple, it has the problem that the accumulation rate of the monomolecular film on the solid carrier is poor.

第2図に例示した水平付着方式の成膜装置の基本構成は
、平板状等の固体担体を単分子膜の展開されている液面
上に平行に接触させることにより、固体担体上に単分子
膜又は単分子累積膜を成膜するものである。この水平付
着方式では、累積率はほぼ100%であるが、固体担体
の上下装置が複雑になるという問題があった。
The basic configuration of the horizontal deposition type film forming apparatus illustrated in Fig. 2 is to bring a solid support such as a flat plate into parallel contact with the liquid surface on which a monomolecular film is being developed, thereby forming a single molecule on the solid support. A film or a monomolecular cumulative film is formed. In this horizontal deposition method, the accumulation rate is almost 100%, but there is a problem that the apparatus for raising and lowering the solid carrier becomes complicated.

円筒回転方式の基本構成は1円筒状等の固体担体を、単
分子膜の展開されている液面上で回転させることにより
、円筒形相体上に単分子膜又は単分子累積膜を成膜する
ものである。この回転円筒法では上記の2方式とは異り
、第3図(a)〜(c)で示す如く円筒を境界として左
右に異なる単分子膜を展開すれば、1回の動作で単分子
膜を累積することができるという長所がある。しかしな
がら、円筒回転方式では以下のような問題があった。例
えば第3図(a)の如く、円筒中心Cがほぼ液面と同じ
高さにある時には、円筒への単分子膜の移しとりの様子
は垂直浸漬方式と同様であり、累積率が低下してしまう
The basic structure of the cylindrical rotation method is to form a monomolecular film or a monomolecular cumulative film on a cylindrical phase body by rotating a cylindrical solid support above the liquid surface where the monomolecular film is being developed. It is something. This rotating cylinder method differs from the above two methods in that, as shown in Figures 3(a) to (c), different monomolecular films can be spread on the left and right sides with the cylinder as the boundary. It has the advantage of being able to accumulate. However, the cylindrical rotation method has the following problems. For example, as shown in Figure 3(a), when the cylinder center C is at almost the same height as the liquid level, the transfer of the monomolecular film to the cylinder is similar to the vertical immersion method, and the accumulation rate decreases. I end up.

また、第3図(b)の如く、円筒中心Cが液面より高い
場合にも累積率は低下してしまう。これは、次のような
理由による。円筒2より左側にある黒丸で示した分子1
2が液面から円筒2に移し取られる際には、移し取られ
る部分における分子の動きを説明するために示した第3
図(f)における如くに、黒丸分子はわずかに回転する
(θ<90’)だけであり、従って円筒2上に無理なく
付着することができ、この部分の累積率は大となる。し
かしながら、右側の白丸で示した分子11は、第3図(
g)に示す如くに相当回転(θン90°)する。円筒中
心Cが液面より高ければ高いほど回転は大となる。この
急激な回転によって分子に無理がかかること、また液面
上の分子の疎・水幕(図中占で示した分子の直線部分)
と円筒2トの分子の疎水基同志が向き合う度合が大とな
り、円筒2上の分子が液面上の分子に引っ張られ剥離し
やすくなること等により累積率が小となり、全体として
は累積率が低下してしまう。
Furthermore, as shown in FIG. 3(b), the accumulation rate also decreases when the cylinder center C is higher than the liquid level. This is due to the following reasons. Molecule 1 shown by a black circle on the left side of cylinder 2
When 2 is transferred from the liquid surface to the cylinder 2, the third point shown to explain the movement of molecules in the part where it is transferred is
As shown in Figure (f), the black circle molecules rotate only slightly (θ<90'), and therefore can be easily attached to the cylinder 2, and the accumulation rate in this portion is large. However, the molecule 11 shown in the white circle on the right side is
As shown in g), it rotates considerably (θ-90°). The higher the cylinder center C is above the liquid level, the greater the rotation. This sudden rotation puts stress on the molecules, and the sparse/water curtain of the molecules on the liquid surface (the straight line part of the molecules shown in the diagram)
The degree to which the hydrophobic groups of the molecules on the cylinder 2 face each other increases, and the molecules on the cylinder 2 are pulled by the molecules on the liquid surface and easily peel off, resulting in a small accumulation rate, and the overall accumulation rate is It will drop.

また、第3図(C)の如く、円筒中心Cが液面より低い
場合には、第3図(b)と逆で、円筒2より右側にある
白丸で示した分子は累積率が高く(第3図(h)参照)
、左側にある黒丸で示した分子は累積率が低下してしま
う(第3図(i)参照)。
Furthermore, as shown in Figure 3(C), when the cylinder center C is lower than the liquid level, contrary to Figure 3(b), molecules indicated by white circles on the right side of the cylinder 2 have a high accumulation rate ( (See Figure 3 (h))
, the accumulation rate of the molecules indicated by the black circles on the left side decreases (see FIG. 3(i)).

上述した如く円筒回転方法では、円筒2を境界として区
分されている単分子膜を同時に移し取ろうとする場合に
は、累積率の点で問題があった。
As described above, in the cylinder rotation method, there is a problem in terms of the accumulation rate when trying to simultaneously transfer the monomolecular films divided by the cylinder 2 as a boundary.

(3)発明の開示 本発明は上記の事実に鑑み成されたものであって、本発
明の目的は、上記問題点を解消した新規な成膜装置を提
供することにある。
(3) Disclosure of the Invention The present invention has been made in view of the above facts, and an object of the present invention is to provide a novel film forming apparatus that solves the above problems.

本発明の目的は、以下の本発明によって達成される。The objects of the present invention are achieved by the following invention.

成膜用分子群を展開する為の液槽を備え、前記液槽中に
収容する液体に液面差が生じるように前記液槽を構成し
たことを特徴とする成膜装置。
A film forming apparatus comprising a liquid tank for developing a group of molecules for film forming, and the liquid tank is configured so that a difference in liquid level occurs in the liquid contained in the liquid tank.

(4)発明を実施するための最良の形態以下、第4図〜
第6図に示す実施例装置をもとにして、本発明について
詳細に説明する。尚、以下の例では説明を簡略化するた
め、担体を円筒とした場合について主として説明する。
(4) Best mode for carrying out the invention Below, Figure 4~
The present invention will be explained in detail based on the embodiment shown in FIG. In the following example, in order to simplify the explanation, the case where the carrier is a cylinder will be mainly explained.

第4図〜第6図は1本発明に係る成膜装置の実施例であ
り、その略示的縦断面図を示している。
FIGS. 4 to 6 show an embodiment of a film forming apparatus according to the present invention, and show schematic longitudinal cross-sectional views thereof.

第4図〜第6図において、3.4はその表面に単分子膜
を形成させる液体、例えば水、エタノール等であり、l
は液体3.4を溜めるための液槽である。2は円筒形相
体であり、着脱可能な固定機構(不図示)により液槽1
に保持され、モーター等の駆動手段(不図示)により正
逆回転可能にされている。5は液槽l内の液体3.4を
円筒2を境界として区分するためのしきり板、例えばゴ
ムブレード、テフロンブレード等である。6は浸透圧の
高い液体、7は浸透圧の低い液体、8はしきり板5と同
様に液槽l内の液体6.7を円筒2を境界として区分す
るための半透膜である。9は3゜4と同様に単分子膜を
展開する液体、10は9より比重が小さくかつ分子を溶
解しない液体である。
In Figures 4 to 6, 3.4 is a liquid that forms a monomolecular film on its surface, such as water, ethanol, etc.
is a liquid tank for storing liquid 3.4. 2 is a cylindrical companion body, which is connected to the liquid tank 1 by a detachable fixing mechanism (not shown).
It is held in place and can be rotated in forward and reverse directions by a driving means (not shown) such as a motor. Reference numeral 5 denotes a partition plate, such as a rubber blade or a Teflon blade, for dividing the liquid 3.4 in the liquid tank 1 using the cylinder 2 as a boundary. 6 is a liquid with high osmotic pressure, 7 is a liquid with low osmotic pressure, and 8 is a semipermeable membrane for dividing the liquid 6.7 in the liquid tank 1 using the cylinder 2 as a boundary, similar to the partition plate 5. 9 is a liquid that develops a monomolecular film like 3°4, and 10 is a liquid that has a lower specific gravity than 9 and does not dissolve molecules.

以下、第4図〜第6図に示した実施例について順を追っ
て説明する。
Hereinafter, the embodiments shown in FIGS. 4 to 6 will be explained in order.

第4図の装置は、単分子膜の展開される液面に高低差を
つけるための手段として、しきり板を利用した例である
。第4図の装置においては、円筒2を図のようにセット
した後、円筒2およびしきり板5によって区分される液
槽l内のそれぞれの部分A、Hに、液面の高低差が生じ
るように不図示の注入口から液体3および4を注入する
。図では液槽l内の部分Bに入れられている液体3の液
面を、Aに入れられている液体4の液面よりも低くしで
ある。液体3.4を注入した後、単分子膜を液体3.4
のそれぞれの液面上に展開して、円筒2を図の矢印方向
(反時計方向)に回転させれば、円筒2上に累積率の向
上したしかも所望の累積度の単分子膜から成る単分子累
積膜を得ることができる。
The apparatus shown in FIG. 4 is an example in which a partition plate is used as a means for creating a height difference in the liquid surface on which a monomolecular film is spread. In the apparatus shown in FIG. 4, after the cylinder 2 is set as shown in the figure, a height difference in the liquid level is created in each part A and H in the liquid tank l divided by the cylinder 2 and the partition plate 5. Liquids 3 and 4 are injected from injection ports (not shown). In the figure, the liquid level of liquid 3 contained in part B in liquid tank l is lower than the liquid level of liquid 4 contained in part A. After injecting liquid 3.4, the monolayer was injected into liquid 3.4.
By rotating the cylinder 2 in the direction of the arrow in the figure (counterclockwise), a monolayer consisting of a monomolecular film with an improved accumulation rate and a desired degree of accumulation is deposited on the cylinder 2. A molecular cumulative film can be obtained.

すなわち、従来例では液面差がないために、第3図に示
した如く、液面から単分子膜を移し取る際の分子の回転
が円筒2の回転方向の一方の側では大きくなるために、
累積率が低下していたが。
That is, in the conventional example, since there is no difference in liquid level, the rotation of the molecules when transferring the monomolecular film from the liquid level becomes larger on one side in the direction of rotation of the cylinder 2, as shown in FIG. ,
Although the cumulative rate was decreasing.

上記構成によればA、B両方の部分で分子の回転を小さ
くすることができるので累積率の向上をはかることがで
きる。従って、液槽l内の部分Bに入れる液体4の液面
を、Aに入れる液体3の液面よりも低くするのであれば
、円筒2の回転方向を図の如く反時計方向とし、一方、
液体4の液面を液体3の液面より高くするのであれば、
円筒2の回転方向を時計方向とするのが好ましい。
According to the above configuration, since the rotation of molecules can be reduced in both parts A and B, it is possible to improve the accumulation rate. Therefore, if the level of liquid 4 to be placed in part B in liquid tank l is to be lower than the level of liquid 3 to be placed in part A, the direction of rotation of cylinder 2 should be counterclockwise as shown in the figure, and on the other hand,
If you want to make the liquid level of liquid 4 higher than the liquid level of liquid 3,
Preferably, the direction of rotation of the cylinder 2 is clockwise.

液槽l内の部分A、Hに液面の高低差が生じるように入
れられる液体3,4の量としては、例えば液面の高い方
の液体、図ではAの側の液体3があまり多すぎると液体
3及びその上に展開されての液体、図では液体4及びそ
の上に展開されている分子12に混入してしまうし、ま
た液体4があまり少なすぎると、円筒2と液体の接触面
積が少なくなって累積率が下がるし、液体4をさらに少
なくすると液体4と円筒2が接触しなくなるので、円筒
の半径をrとすると液体3,4の液面の高さり、h’は
、円筒中心cft基準としテ(1/3) rと(213
)rの間とするのが好ましい。もちろん1 hとhoは同□じ値とすることもできるし、異る値とす
ることも可能である。
As for the amount of liquids 3 and 4 that are put into parts A and H in the liquid tank l so that there is a difference in the height of the liquid level, for example, the liquid with the higher liquid level, the liquid 3 on the A side in the figure, is too large. If it is too small, it will mix with the liquid 3 and the liquid spread on it (in the figure, the liquid 4 and the molecules 12 spread on it), and if there is too little liquid 4, the cylinder 2 and the liquid will not come into contact with each other. The area decreases and the accumulation rate decreases, and if the amount of liquid 4 is further reduced, liquid 4 and cylinder 2 will not come into contact with each other, so if the radius of the cylinder is r, the height of the liquid level of liquids 3 and 4, h', will be: Using the cylinder center cft as a reference, Te (1/3) r and (213
) r. Of course, 1h and ho can be the same value or can be different values.

液槽l内の部分A、Hに入れる液体3,4としては、所
望に応じて上記のような水、エタノール等を使用するこ
とが可能であるが、液体3,4を同じものとすることも
できるし、また異る液体を使用してもよい、液体3,4
に展開する成膜用分子群11.12としては、液体3.
4上に単分子膜を形成し得る分子、例えばその分子内に
親木基および疎水機を有するような分子であれば使用す
ることができるが、液体3,4に展開する分子は同じも
のとしてもよいし、異る種類の分子とすることもできる
。もちろん、2種以上の分子を液体3゜4上に展開して
混合単分子累積膜を成膜する等のことも可能である。
As the liquids 3 and 4 to be put in parts A and H in the liquid tank 1, water, ethanol, etc. as mentioned above can be used as desired, but liquids 3 and 4 should be the same. You can also use different liquids.Liquids 3 and 4
The film-forming molecule group 11.12 developed in liquid 3.
Any molecule that can form a monomolecular film on 4 can be used, for example, a molecule that has a parent tree group and a hydrophobic group within the molecule, but the molecules that develop in liquids 3 and 4 are the same. It can also be a different type of molecule. Of course, it is also possible to form a mixed monomolecular cumulative film by developing two or more types of molecules on a liquid 3.4.

なお、仕切り板5は、液体3と液体4が、液槽l内の部
分AとBとの間を移動しないようにする為のものである
ので、ゴムブレードあるいはテフロンブレードなどの気
密性の高いものを用いるのが好ましい。
The partition plate 5 is to prevent the liquid 3 and liquid 4 from moving between parts A and B in the liquid tank l, so it is made of a highly airtight material such as a rubber blade or a Teflon blade. It is preferable to use

第5図の装置は、単分子膜の展開される液面に高低差を
つけるための手段として浸透圧の差を利用した例である
。このため、本例においては第4図におけるしきり板5
に相当する部分を半透膜8とし、該半透膜8と円筒2と
で液槽1内をA、B2つの部分に区分し、AおよびBの
どちらか一方に入れる液体を浸透圧の低い液体(図では
Bに入れられている液体7を浸透圧の低い液体としであ
る)とし、もラ一方に入れる液体を浸透圧の高い液体(
図ではAに入れられている液体6)とする+−1−−y
k斎−一−1rh/F%W〆一、H(27L−ak’i
?f+1=t−)+r、*せ、第5図におけると同様の
成膜を可能としたものである。
The apparatus shown in FIG. 5 is an example in which a difference in osmotic pressure is used as a means for creating a height difference in the liquid surface on which a monomolecular film is spread. Therefore, in this example, the partition plate 5 in FIG.
The part corresponding to 2 is a semipermeable membrane 8, and the semipermeable membrane 8 and cylinder 2 divide the inside of the liquid tank 1 into two parts A and B, and the liquid to be put into either A or B is a liquid with a low osmotic pressure. A liquid (in the figure, the liquid 7 in B is a liquid with low osmotic pressure), and the liquid in one side is a liquid with high osmotic pressure (
In the figure, the liquid contained in A is 6) +-1--y
ksai-1-1rh/F%W〆1, H(27L-ak'i
? f+1=t-)+r, *S), which makes it possible to form a film similar to that shown in FIG.

一般に浸透圧差によって生じる液面の高低差は、浸透圧
の高い液体、本例の場合液体。6の体積に反比例するの
で、浸透圧の高い液体を入れる方の液槽l、円筒2及び
半透lI!8によって囲まれる部分、本例の場合はAの
体積を浸透圧の低い液体を入れる方の体積、本例の場合
はBより小さくするのが好ましい、浸透圧の高い液体と
しては、水などの溶媒に、その溶媒に可溶の溶質、例え
ば砂糖や金属塩などを溶かした溶液等が利用し得るもの
として挙げられ、浸透圧の低い液体7としては、上記の
水などの溶媒が利用し得るものとして挙げられるが、液
体6の溶媒と液体7の溶媒は同一とするのが好ましい。
Generally, the height difference in liquid level caused by a difference in osmotic pressure is caused by a liquid with a high osmotic pressure, in this case a liquid. Since it is inversely proportional to the volume of 6, the liquid tank l, cylinder 2 and semipermeable lI which contain the liquid with high osmotic pressure! It is preferable that the volume of the part surrounded by 8, A in this example, be smaller than the volume of the liquid containing the low osmotic pressure, B in this example.As the liquid with high osmotic pressure, water etc. A solution in which a solute soluble in the solvent, such as sugar or a metal salt, is dissolved in the solvent can be used, and as the liquid 7 with low osmotic pressure, the above-mentioned solvents such as water can be used. However, it is preferable that the solvent of liquid 6 and the solvent of liquid 7 are the same.

また、本例の場合にも第4図におけると同様に、液体6
及び液体7の液面の高さh及びhoは、円筒2の半径r
に対し、円筒中心Cを基準として、(1/3) rと(
2/3) rの間とするのが好ましい、また、浸透圧は
溶液の濃度に比例するので、液面の高低差の調節は、溶
液6の濃度を変化させる事により行なうのが簡便である
。 さらに、半透膜8は、溶媒のみを透過し、溶液中の
溶質を透過しないものを、溶媒にあわせて適宜選択する
ことができるが、例えばコロジオン膜等、一般に広く知
られているものを適宜使用することが可能である。また
半透膜8は、第4図における仕切り板5と同様に液体6
と液体7との混入を防止する目的もあるので、第5図に
おけると同様に半透膜8と円筒2の間にすき間ができな
いようにしである。
Also in this example, as in FIG. 4, the liquid 6
and the height h and ho of the liquid level of the liquid 7 are the radius r of the cylinder 2.
On the other hand, with the cylinder center C as a reference, (1/3) r and (
2/3) It is preferable to set it between r. Also, since the osmotic pressure is proportional to the concentration of the solution, it is convenient to adjust the difference in height of the liquid level by changing the concentration of the solution 6. . Further, the semipermeable membrane 8 can be appropriately selected depending on the solvent, such that it only allows the solvent to pass through and does not allow the solute in the solution to pass through. It is possible to use. Further, the semipermeable membrane 8 is used for liquid 6, similar to the partition plate 5 in FIG.
Since the purpose is also to prevent mixing of the liquid 7 with the semipermeable membrane 8 and the liquid 7, a gap is not formed between the semipermeable membrane 8 and the cylinder 2, as in FIG.

第6図の装置は、単分子膜の展開される液面に高低差を
つけるための手段として、液体の比重差を利用した例で
ある。第6図の装置においては、第4図におけるしきり
板5をなくし、単分子膜の展開される液面(図では液体
9の液面)を区分し、該液面に分子を展開した後、円筒
2で区分される液面のどちらか一方の側(図に向って左
側)に単分子膜の展開されている液体9よりも比重の軽
い液体(図では液体10)を入れることで、液槽1内の
単分子膜が展開される液体9に液面差を生じさせ、第4
図におけると同様の成膜を可能にしたものである。
The apparatus shown in FIG. 6 is an example in which a difference in specific gravity of a liquid is used as a means for creating a height difference in the liquid surface on which a monomolecular film is spread. In the apparatus shown in FIG. 6, the partition plate 5 in FIG. 4 is eliminated, the liquid surface on which the monomolecular film is spread (the liquid surface of liquid 9 in the figure) is divided, and after the molecules are spread on the liquid surface, By placing a liquid (liquid 10 in the figure) with a lighter specific gravity than the liquid 9 on which the monomolecular film is spread on either side of the liquid surface divided by the cylinder 2 (on the left side when facing the figure), the liquid A liquid level difference is created in the liquid 9 in which the monomolecular film in the tank 1 is developed, and the fourth
This makes it possible to form a film similar to that shown in the figure.

すなわち液体9は、分子11.12をその表面に展開す
るための液体であり、液体10は液体9に液面差を生じ
させるための液体である。従って、液体lOとしては液
体9よりも比重が軽くかつ液体lOと9との界面に展開
されている分子12を溶かすことなく、しかも液体9と
混じりあわず液体9との境界に単分子膜を形成し得る液
体を用いる必要がある。単分子膜を展開する液体9とし
ては前述の水等が利用し得るが、液体9に液面差を生じ
させる液体10としては石油エーテル等が利用し得るも
のとして挙げられる。
That is, the liquid 9 is a liquid for spreading the molecules 11 and 12 on its surface, and the liquid 10 is a liquid for causing a liquid level difference in the liquid 9. Therefore, the liquid IO has a lighter specific gravity than the liquid 9, does not dissolve the molecules 12 spread out at the interface between the liquid IO and 9, and does not mix with the liquid 9, forming a monomolecular film at the boundary with the liquid 9. It is necessary to use a liquid that can be formed. As the liquid 9 that develops the monomolecular film, the water described above can be used, but as the liquid 10 that causes a difference in the liquid level in the liquid 9, petroleum ether or the like can be used.

尚、前記実施例以外にも、例えば円筒2で区分される液
槽lのそれぞれの部分を気密構造として、圧力差を利用
する事により液面に高低差をつける等の事も可能である
。また、上記実施例では円筒2を1つとしであるが、液
槽l内に複数の円筒を並列に設置する等の事も可能であ
る。
In addition to the above-mentioned embodiment, it is also possible to make the liquid tank 1 divided by the cylinder 2 into an airtight structure so as to create a height difference in the liquid level by utilizing a pressure difference. Further, in the above embodiment, only one cylinder 2 is used, but it is also possible to install a plurality of cylinders in parallel within the liquid tank l.

以上、相体を円筒形相体とした場合を例とじて本発明を
説明したが、本発明の装置は上記例に限定されるもので
ないことは言うまでもない、また、担体としても、上記
円筒の他、角柱状、球状等の担体、あるいはこれら担体
上に着脱可能に取り付けたシート状の担体等にも同様の
ことが言える。更にはシート状等の担体を、例えばベル
トコンベアにおけるように2つの円筒間にわたして成膜
する等の場合についても同様のことが言える。
The present invention has been explained above using the case where the partner body is cylindrical, but it goes without saying that the device of the present invention is not limited to the above example. The same can be said of prismatic, spherical, etc. carriers, or sheet-like carriers removably attached to these carriers. Furthermore, the same can be said of the case where a film is formed by passing a sheet-like carrier between two cylinders, such as on a belt conveyor.

また、連続シート状等の担体をロール状に巻き取り、こ
れを2本の円筒間にわたして連続的に成膜する等の場合
にも同様のことが言える。
The same thing can also be said when a carrier such as a continuous sheet is wound up into a roll and passed between two cylinders to form a film continuously.

以上に説明した如く、本発明の成膜装置によれば、単分
子膜の展開される液面に高低差を設けることが可能であ
り、従って液面から単分子膜を移し取る際の分子の回転
を小さくすることができるので、累積率の向上が可能と
なった。
As explained above, according to the film forming apparatus of the present invention, it is possible to provide a height difference in the liquid surface on which a monomolecular film is developed, and therefore, when transferring a monomolecular film from the liquid surface, it is possible to create a height difference. Since the rotation can be reduced, the accumulation rate can be improved.

【図面の簡単な説明】[Brief explanation of drawings]

第1図〜第3図は、それぞれ順に垂直浸漬方式、水平付
着方式および円筒回転方式の成膜装置における成膜状態
を説明する図、第4図〜第6図は本発明に係る成膜装置
の実施例の略示的縦断面図である。 1−−一液槽 2−m−円筒 3 、4 、6 、7 、9 、10−−一 液体5.
14−−−Lきり板 8−m−半透膜 11、12−m−分子 13−m−平板状担体 第3図(9) 第3図(C) 第3図(h) 第3図(i) 第4図 第5図 第6図
FIGS. 1 to 3 are diagrams illustrating the film forming state in a vertical immersion type, horizontal deposition type, and cylindrical rotation type film forming apparatus, respectively, and FIGS. 4 to 6 are views showing a film forming apparatus according to the present invention. 1 is a schematic longitudinal sectional view of an embodiment of FIG. 1--Liquid tank 2-m-Cylinder 3, 4, 6, 7, 9, 10--Liquid 5.
14--L-cut plate 8-m-semipermeable membrane 11, 12-m-molecules 13-m-plate-shaped carrier Fig. 3 (9) Fig. 3 (C) Fig. 3 (h) Fig. 3 ( i) Figure 4 Figure 5 Figure 6

Claims (1)

【特許請求の範囲】[Claims] 成膜用分子群を展開する為の液槽を備え、前記液槽中に
収容する液体に液面差が生じるように前記液槽を構成し
たことを特徴とする成膜装置。
A film forming apparatus comprising a liquid tank for developing a group of molecules for film forming, and the liquid tank is configured so that a difference in liquid level occurs in the liquid contained in the liquid tank.
JP4718284A 1984-03-14 1984-03-14 Film forming device Pending JPS60193530A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP4718284A JPS60193530A (en) 1984-03-14 1984-03-14 Film forming device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP4718284A JPS60193530A (en) 1984-03-14 1984-03-14 Film forming device

Publications (1)

Publication Number Publication Date
JPS60193530A true JPS60193530A (en) 1985-10-02

Family

ID=12767940

Family Applications (1)

Application Number Title Priority Date Filing Date
JP4718284A Pending JPS60193530A (en) 1984-03-14 1984-03-14 Film forming device

Country Status (1)

Country Link
JP (1) JPS60193530A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH04124910U (en) * 1991-04-23 1992-11-13 凸版印刷株式会社 assembly container
US5512326A (en) * 1991-06-12 1996-04-30 Canon Kabushiki Kaisha Method and apparatus for forming monomolecular film or built-up monomolecular film
JP4759616B2 (en) * 2005-07-01 2011-08-31 ピーピージー インダストリーズ オハイオ, インコーポレイテッド Transparent electrodes for electrochromic switchable cells

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH04124910U (en) * 1991-04-23 1992-11-13 凸版印刷株式会社 assembly container
US5512326A (en) * 1991-06-12 1996-04-30 Canon Kabushiki Kaisha Method and apparatus for forming monomolecular film or built-up monomolecular film
JP4759616B2 (en) * 2005-07-01 2011-08-31 ピーピージー インダストリーズ オハイオ, インコーポレイテッド Transparent electrodes for electrochromic switchable cells

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