JP5518406B2 - Method for producing fine particle array structure - Google Patents
Method for producing fine particle array structure Download PDFInfo
- Publication number
- JP5518406B2 JP5518406B2 JP2009209244A JP2009209244A JP5518406B2 JP 5518406 B2 JP5518406 B2 JP 5518406B2 JP 2009209244 A JP2009209244 A JP 2009209244A JP 2009209244 A JP2009209244 A JP 2009209244A JP 5518406 B2 JP5518406 B2 JP 5518406B2
- Authority
- JP
- Japan
- Prior art keywords
- groove
- fine particle
- fine particles
- solvent
- fine
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Fee Related
Links
Landscapes
- Application Of Or Painting With Fluid Materials (AREA)
- Other Surface Treatments For Metallic Materials (AREA)
Description
本発明は、微粒子配列構造体及びその製造方法に関し、より詳細には、基板に形成された溝の内壁に、微粒子が集合して規則的に配列した微粒子配列構造体を形成させる技術に関する。 The present invention relates to a fine particle array structure and a method for manufacturing the same, and more particularly to a technique for forming a fine particle array structure in which fine particles are gathered and regularly arranged on an inner wall of a groove formed in a substrate.
数nm〜数μm程度の粒径の微粒子を集合して規則的に配列させてその配列構造を形成させる方法としては、微粒子を個々にマニピュレートする手法も考えられるが、工業的な応用のためには、微粒子の自己組織化現象を利用するのが現実的である。微粒子の自己組織化現象とは、すなわち、微粒子を溶媒に懸濁した微粒子懸濁液を基板に載置して、その溶媒を蒸発させていくと、溶媒の膜厚が微粒子の基板からの高さをぎりぎり満たす程度にまで小さくなった部分(メニスカス先端部)の蒸発に伴う溶媒の流れと溶媒の表面張力とによって、微粒子が個々に順次集合していく現象である。例えば下記特許文献1には、そのような微粒子の自己組織化現象を利用した微粒子薄膜の製造方法が記載されている。 As a method of collecting and regularly arranging fine particles having a particle diameter of several nm to several μm to form the arrangement structure, a method of individually manipulating the fine particles can be considered, but for industrial applications. It is realistic to use the self-organization phenomenon of fine particles. The self-organization phenomenon of fine particles means that when a fine particle suspension in which fine particles are suspended in a solvent is placed on a substrate and the solvent is evaporated, the film thickness of the solvent increases from the fine particle substrate. This is a phenomenon in which fine particles are successively collected individually by the flow of the solvent and the surface tension of the solvent accompanying the evaporation of the portion (meniscus tip) that has become small enough to fill the gap. For example, Patent Document 1 below describes a method for producing a fine particle thin film using such a self-organization phenomenon of fine particles.
しかし、従来、フラットな基板に微粒子の配列集合体を形成させて2次元的な構造体とする技術の蓄積はあったが、これらの微粒子の配列集合体を3次元的な構造体とする技術の蓄積は乏しく、数百nm〜数百μm程度、深さ数μm〜1mm程度のいわゆるマイクロチャネルと呼ばれる微細溝構造の溝の内壁に、微粒子の配列集合体を形成させることは、技術的に難しかった。 Conventionally, however, there has been accumulation of technology for forming a two-dimensional structure by forming an array of fine particles on a flat substrate. It is technically difficult to form an array aggregate of fine particles on the inner wall of a so-called microchannel structure called a microchannel having a depth of about several hundred nm to several hundred μm and a depth of about several μm to 1 mm. was difficult.
このような問題に対して、下記特許文献2において、微粒子懸濁液の微粒子の数量を調整してマイクロチャネルの内壁に微粒子の配列集合体を形成させる微粒子アセンブル法が記載されている。 In order to solve such a problem, the following Patent Document 2 describes a fine particle assembly method in which the number of fine particles in a fine particle suspension is adjusted to form an array aggregate of fine particles on the inner wall of a microchannel.
しかしながら、上記特許文献2に記載された技術は、溝構造の内壁の選択された所定の壁部にのみ微粒子の配列集合体を形成させることに適した技術ではなかった。 However, the technique described in Patent Document 2 is not a technique that is suitable for forming an array aggregate of fine particles only on a selected predetermined wall portion of the inner wall of the groove structure.
したがって、本発明の目的は、溝構造の内壁の選択された所定の壁部にのみ微粒子の配列集合体を形成させる技術を提供することにある。 Accordingly, an object of the present invention is to provide a technique for forming an array aggregate of fine particles only on a selected predetermined wall portion of an inner wall of a groove structure.
上記目的を達成するにあたり、本発明は、以下の構成を有する微粒子配列構造体及びその製造方法を提供する。
[1] 基板に形成された溝の選択された所定の壁部にのみ、微粒子が単層又は複数層で配列して形成されていることを特徴とする微粒子配列構造体。
[2] 前記基板は、シリコン、ガラス、アルミナ、ITO、プラスチック、又はポリカーボネートから選ばれたものである[1]記載の微粒子配列構造体。
[3] 前記溝は、幅0.1〜100μm、深さ5〜600μmである[1]又は[2]記載の微粒子配列構造体。
[4] 前記微粒子は、粒径が1nm〜5μmである[1]〜[3]のいずれか1つに記載の微粒子配列構造体。
[5] 前記微粒子の材料は、金(Au)、銀(Ag)、銅(Cu)、白金(Pt)、アルミ(Al)、パラジウム(Pd)、ニッケル(Ni)、コバルト(Co)等の金属、酸化錫(SnO2)、酸化亜鉛(ZnO)、酸化チタン(TiO2)、酸化ケイ素(SiO2)、FeO3、CdO、SrTiO3、CoO、Fe3O4、Cu2O、MgO、MnO、Ag2O、In2O3、WO3等の金属酸化物、又はポリスチレン、アクリル樹脂等の有機ポリマーである[1]〜[4]のいずれか1つに記載の微粒子配列構造体。
[6] 表面に所定の幅及び深さを有する溝が形成された基板の該溝に、微粒子を溶媒に懸濁してなる微粒子懸濁液を充填し、前記充填した微粒子縣濁液の溶媒を乾燥させることにより、前記溝の壁部に、前記微粒子が単層又は複数層で配列してなる該微粒子の配列集合体を形成させる微粒子配列構造体の製造方法であって、前記微粒子が懸濁した溶媒の前記溝の壁部に対するメニスカス先端部が、前記溝の壁部の選択された所定の領域のみを移動するようにして、前記溝の選択された所定の壁部にのみ、前記微粒子の配列集合体を形成させることを特徴とする微粒子配列構造体の製造方法。
[7] 前記微粒子懸濁液として前記微粒子の前記溶媒に対する体積率が所定の値の該微粒子懸濁液を用いることにより、前記溝の選択された所定の壁部にのみ、前記微粒子の配列集合体を形成させる[6]記載の微粒子配列構造体の製造方法。
[8] 前記溝に前記微粒子懸濁液を充填した後、前記充填した微粒子縣濁液の溶媒を所定の温度、湿度、及び/又は気圧下で乾燥させることにより、前記溝の選択された所定の壁部にのみ、前記微粒子の配列集合体を形成させる[6]記載の微粒子配列構造体の製造方法。
[9] 前記溝の選択された所定の壁部以外の該壁部の、前記微粒子縣濁液の溶媒に対する濡れ性を、前記選択された壁部よりも小さくすることにより、前記溝の選択された所定の壁部にのみ、前記微粒子の配列集合体を形成させる[6]記載の微粒子配列構造体の製造方法。
[10] 前記基板を前記溝の少なくとも一部が該微粒子懸濁液に接触するように浸漬させることにより、毛細管現象によって前記微粒子縣濁液を前記溝に充填し、次いで前記基板を引き上げて前記基板を乾燥させる[6]〜[9]のいずれか1つに記載の微粒子配列構造体の製造方法。
[11] 前記基板は、シリコン、ガラス、アルミナ、ITO、プラスチック、又はポリカーボネートから選ばれたものである[6]〜[10]のいずれか1つに記載の微粒子配列構造体の製造方法。
[12] 前記溝は、幅0.1〜100μm、深さ5〜600μmである[6]〜[11]のいずれか1つに記載の微粒子配列構造体の製造方法。
[13] 前記微粒子は、粒径が1nm〜5μmである[6]〜[12]のいずれか1つに記載の微粒子配列構造体の製造方法。
[14] 前記微粒子の材料は、金(Au)、銀(Ag)、銅(Cu)、白金(Pt)、アルミ(Al)、パラジウム(Pd)、ニッケル(Ni)、コバルト(Co)等の金属、酸化錫(SnO2)、酸化亜鉛(ZnO)、酸化チタン(TiO2)、酸化ケイ素(SiO2)、FeO3、CdO、SrTiO3、CoO、Fe3O4、Cu2O、MgO、MnO、Ag2O、In2O3、WO3等の金属酸化物、又はポリスチレン、アクリル樹脂等の有機ポリマーである[6]〜[13]のいずれか1つに記載の微粒子配列構造体の製造方法。
[15] 前記溝の選択された所定の壁部に対する前記微粒子の充填率(ε)が所望の値となるように、下記数式(1)に基づいて設定した条件で、前記溝に充填した前記微粒子縣濁液の溶媒を乾燥させる、[6]〜[14]のいずれか1つに記載の微粒子配列構造体の製造方法。
In achieving the above object, the present invention provides a fine particle array structure having the following constitution and a method for producing the same.
[1] A fine particle array structure in which fine particles are formed in a single layer or a plurality of layers only on a predetermined wall portion of a groove formed in a substrate.
[2] The fine particle array structure according to [1], wherein the substrate is selected from silicon, glass, alumina, ITO, plastic, or polycarbonate.
[3] The fine particle array structure according to [1] or [2], wherein the groove has a width of 0.1 to 100 μm and a depth of 5 to 600 μm.
[4] The fine particle array structure according to any one of [1] to [3], wherein the fine particles have a particle diameter of 1 nm to 5 μm.
[5] The material of the fine particles is gold (Au), silver (Ag), copper (Cu), platinum (Pt), aluminum (Al), palladium (Pd), nickel (Ni), cobalt (Co), etc. Metal, tin oxide (SnO 2 ), zinc oxide (ZnO), titanium oxide (TiO 2 ), silicon oxide (SiO 2 ), FeO 3 , CdO, SrTiO 3 , CoO, Fe 3 O 4 , Cu 2 O, MgO, MnO, Ag 2 O, in 2 O 3, WO metal oxides such as 3, or polystyrene, an organic polymer such as an acrylic resin [1] to fine particle arrangement structure according to any one of [4].
[6] A fine particle suspension obtained by suspending fine particles in a solvent is filled in the grooves of a substrate having grooves having a predetermined width and depth on the surface, and the solvent of the filled fine particle suspension is used. A method for producing a fine particle array structure in which the fine particles are arranged in a single layer or a plurality of layers to form an array aggregate of the fine particles on a wall portion of the groove by drying, wherein the fine particles are suspended. The meniscus tip portion of the solvent with respect to the groove wall portion moves only in the selected predetermined region of the groove wall portion, so that the fine particles are applied only to the selected predetermined wall portion of the groove. A method for producing a fine particle array structure, wherein an array aggregate is formed.
[7] By using the fine particle suspension in which the volume ratio of the fine particles to the solvent is a predetermined value as the fine particle suspension, the array of fine particles is arranged only on a predetermined wall portion of the groove. The method for producing a fine particle array structure according to [6], wherein a body is formed.
[8] After filling the groove with the fine particle suspension, the solvent of the filled fine particle suspension is dried under a predetermined temperature, humidity, and / or atmospheric pressure to thereby select the predetermined groove. [6] The method for producing a fine-particle array structure according to [6], wherein the fine-particle array aggregate is formed only on the wall portion.
[9] The groove is selected by making wettability of the wall portion other than the selected predetermined wall portion of the groove with respect to the solvent of the fine particle suspension smaller than that of the selected wall portion. The method for producing a fine particle arrangement structure according to [6], wherein the fine particle arrangement aggregate is formed only on a predetermined wall portion.
[10] By immersing the substrate so that at least a part of the groove is in contact with the fine particle suspension, the fine particle suspension is filled into the groove by capillary action, and then the substrate is pulled up to The method for producing a fine particle array structure according to any one of [6] to [9], wherein the substrate is dried.
[11] The method for producing a fine particle array structure according to any one of [6] to [10], wherein the substrate is selected from silicon, glass, alumina, ITO, plastic, or polycarbonate.
[12] The method for producing a fine particle array structure according to any one of [6] to [11], wherein the groove has a width of 0.1 to 100 μm and a depth of 5 to 600 μm.
[13] The method for producing a fine particle array structure according to any one of [6] to [12], wherein the fine particles have a particle diameter of 1 nm to 5 μm.
[14] The material of the fine particles is gold (Au), silver (Ag), copper (Cu), platinum (Pt), aluminum (Al), palladium (Pd), nickel (Ni), cobalt (Co), etc. Metal, tin oxide (SnO 2 ), zinc oxide (ZnO), titanium oxide (TiO 2 ), silicon oxide (SiO 2 ), FeO 3 , CdO, SrTiO 3 , CoO, Fe 3 O 4 , Cu 2 O, MgO, MnO, Ag 2 O, in 2 O 3, WO metal oxides such as 3, or polystyrene, an organic polymer such as an acrylic resin [6] to the fine particle arrangement structure according to any one of [13] Production method.
[15] The groove filled in the groove under the conditions set based on the following mathematical formula (1) so that the filling rate (ε) of the fine particles to the predetermined wall portion selected in the groove becomes a desired value. The method for producing a fine particle array structure according to any one of [6] to [14], wherein the solvent of the fine particle suspension is dried.
本発明の微粒子配列構造体によれば、基板に形成された溝の選択された所定の壁部にのみ、微粒子が単層又は複数層で配列して形成されているので、例えば、溝の側壁面のみに導電性を有する金属酸化物の微粒子を配列させ、その微粒子の配列集合体を形成させることで、その金属酸化物の電極を形成し、一方で溝によって形成されている空間に気体が入り込むように構成して、溝の両側壁の電極間に流れる電流に係る抵抗値を測定することによって気体中のガスを感知する、ガスセンサなどに利用できる。 According to the fine particle arrangement structure of the present invention, since the fine particles are formed in a single layer or a plurality of layers only on a predetermined wall portion of the groove formed on the substrate, for example, the groove side By arranging conductive metal oxide fine particles only on the wall surface and forming an array aggregate of the fine particles, an electrode of the metal oxide is formed, while gas is formed in the space formed by the grooves. The gas sensor can be used for a gas sensor or the like that is configured to enter and senses a gas in the gas by measuring a resistance value related to a current flowing between electrodes on both side walls of the groove.
本発明の微粒子配列構造体の製造方法によれば、表面に所定の幅及び深さを有する溝が形成された基板の該溝に、微粒子を溶媒に懸濁してなる微粒子懸濁液を充填し、前記充填した微粒子縣濁液の溶媒を乾燥させることにより、前記溝の壁部に、前記微粒子が単層又は複数層で配列してなる該微粒子の配列集合体を形成させる微粒子配列構造体の製造方法において、前記微粒子が懸濁した溶媒の前記溝の壁部に対するメニスカス先端部が、前記溝の壁部の選択された所定の領域のみを移動するようにして、前記溝の選択された所定の壁部にのみ、前記微粒子の配列集合体を形成させるので、基板に形成された溝の選択された所定の壁部にのみ、微粒子が単層又は複数層で配列して形成されている微粒子配列構造体を、容易に製造することができる。 According to the method for producing a fine particle array structure of the present invention, a fine particle suspension in which fine particles are suspended in a solvent is filled in the groove of a substrate having grooves having a predetermined width and depth on the surface. A fine particle array structure in which the fine particle suspension is dried to form an array aggregate of the fine particles in which the fine particles are arranged in a single layer or a plurality of layers on the wall of the groove. In the manufacturing method, the meniscus tip portion of the solvent in which the fine particles are suspended with respect to the groove wall portion moves only in the selected predetermined region of the groove wall portion. Since the array of fine particles is formed only on the walls of the fine particles, the fine particles are formed by arranging the fine particles in a single layer or a plurality of layers only on the selected predetermined wall portions of the grooves formed on the substrate. An array structure can be easily manufactured. That.
また、本発明の微粒子配列構造体の製造方法においては、前記微粒子の前記溶媒に対する体積率や、前記充填した微粒子縣濁液の溶媒を乾燥させる際の温度、湿度、気圧や、前記微粒子縣濁液の溶媒に対する濡れ性などを、それぞれ所定の値に調整することにより、上記メニスカス先端部が移動する領域を、容易に制御することができる。 Further, in the method for producing a fine particle array structure of the present invention, the volume ratio of the fine particles to the solvent, the temperature, humidity, and pressure when the solvent of the filled fine particle suspension is dried, and the fine particle suspension. By adjusting the wettability of the liquid with respect to the solvent to a predetermined value, it is possible to easily control the region where the meniscus tip moves.
また、本発明の微粒子配列構造体の製造方法においては、前記微粒子の前記溶媒に対する体積率や、前記充填した微粒子縣濁液の溶媒を乾燥させる際の温度、湿度、気圧や、前記微粒子縣濁液の溶媒に対する濡れ性などを、それぞれ所定の値に調整することにより、前記溝の選択された所定の壁部に対する前記微粒子の充填率(ε)を、容易に制御することができる。 Further, in the method for producing a fine particle array structure of the present invention, the volume ratio of the fine particles to the solvent, the temperature, humidity, and pressure when the solvent of the filled fine particle suspension is dried, and the fine particle suspension. By adjusting the wettability of the liquid with respect to the solvent to a predetermined value, the filling rate (ε) of the fine particles with respect to the predetermined wall portion selected in the groove can be easily controlled.
本発明の微粒子配列構造体は、基板に形成された溝の選択された所定の壁部にのみ、微粒子が単層又は複数層で配列して形成されていることを特徴とする。本発明の微粒子配列構造体は、後述する微粒子配列構造体の製造方法によって得ることができる。 The fine particle array structure of the present invention is characterized in that the fine particles are formed in a single layer or a plurality of layers only on a predetermined wall portion of a groove formed in the substrate. The fine particle array structure of the present invention can be obtained by a method for producing a fine particle array structure described later.
本発明の微粒子配列構造体における基板の材質としては、微細溝構造を形成できる基板であれば特に制限を受けないが、シリコン、ガラス、アルミナ、ITO、プラスチック、ポリカーボネートなどを好ましく例示できる。 The material of the substrate in the fine particle array structure of the present invention is not particularly limited as long as it is a substrate capable of forming a fine groove structure, but silicon, glass, alumina, ITO, plastic, polycarbonate and the like can be preferably exemplified.
本発明の微粒子配列構造体における溝の構造としては、幅0.1〜100μm、深さ5〜600μm程度の微細溝構造であることが好ましい。このような微細溝構造の内壁部に微粒子の配列構造体を形成することで、コンパクトで集積化された3次元的構造を有する反応プラットフォームなどに利用できる。 The groove structure in the fine particle array structure of the present invention is preferably a fine groove structure having a width of about 0.1 to 100 μm and a depth of about 5 to 600 μm. By forming an array structure of fine particles on the inner wall of such a fine groove structure, it can be used for a reaction platform having a compact and integrated three-dimensional structure.
本発明の微粒子配列構造体における微粒子としては、粒径が1nm〜5μm程度、より好ましくは粒径が1nm〜100nm程度のものが用いられる。これにより、後述する自己組織化現象を利用した微粒子の配列構造体の形成が容易となる。また、配列構造体の体積あたりの表面積をより大きくすることができ、コンパクトで集積化された3次元的構造を有する反応プラットフォームなどにより適している。 As the fine particles in the fine particle array structure of the present invention, those having a particle size of about 1 nm to 5 μm, more preferably about 1 nm to 100 nm are used. This facilitates formation of an array structure of fine particles using a self-organization phenomenon described later. Further, the surface area per volume of the array structure can be increased, which is more suitable for a reaction platform having a compact and integrated three-dimensional structure.
本発明の微粒子配列構造体における微粒子の材料としては、上記微粒子を構成できるものであれば特に制限を受けないが、金(Au)、銀(Ag)、銅(Cu)、白金(Pt)、アルミ(Al)、パラジウム(Pd)、ニッケル(Ni)、コバルト(Co)等の金属、酸化錫(SnO2)、酸化亜鉛(ZnO)、酸化チタン(TiO2)、酸化ケイ素(SiO2)、FeO3、CdO、SrTiO3、CoO、Fe3O4、Cu2O、MgO、MnO、Ag2O、In2O3、WO3等の金属酸化物、又はポリスチレン、アクリル樹脂等の有機ポリマーなどを好ましく例示できる。 The material of the fine particles in the fine particle array structure of the present invention is not particularly limited as long as it can constitute the fine particles, but gold (Au), silver (Ag), copper (Cu), platinum (Pt), Metals such as aluminum (Al), palladium (Pd), nickel (Ni), cobalt (Co), tin oxide (SnO 2 ), zinc oxide (ZnO), titanium oxide (TiO 2 ), silicon oxide (SiO 2 ), Metal oxides such as FeO 3 , CdO, SrTiO 3 , CoO, Fe 3 O 4 , Cu 2 O, MgO, MnO, Ag 2 O, In 2 O 3 , WO 3 or organic polymers such as polystyrene and acrylic resin Can be preferably exemplified.
一方、本発明の微粒子配列構造体の製造方法は、表面に所定の幅及び深さを有する溝が形成された基板の該溝に、微粒子を溶媒に懸濁してなる微粒子懸濁液を充填し、前記充填した微粒子縣濁液の溶媒を乾燥させることにより、前記溝の壁部に、前記微粒子が単層又は複数層で配列してなる該微粒子の配列集合体を形成させる微粒子配列構造体の製造方法であって、前記微粒子が懸濁した溶媒の前記溝の壁部に対するメニスカス先端部が、前記溝の壁部の選択された所定の領域のみを移動するようにして、前記溝の選択された所定の壁部にのみ、前記微粒子の配列集合体を形成させることを特徴とする。 On the other hand, in the method for producing a fine particle array structure of the present invention, a fine particle suspension obtained by suspending fine particles in a solvent is filled in the groove of a substrate having grooves having a predetermined width and depth on the surface. A fine particle array structure in which the fine particle suspension is dried to form an array aggregate of the fine particles in which the fine particles are arranged in a single layer or a plurality of layers on the wall of the groove. In the manufacturing method, the meniscus tip portion of the solvent in which the fine particles are suspended with respect to the groove wall portion moves only in the selected predetermined region of the groove wall portion, so that the groove is selected. In addition, the fine particle array aggregate is formed only on a predetermined wall portion.
本発明の微粒子配列構造体の製造方法において、「メニスカス先端部」とは、溶媒に懸濁させた微粒子が、溶媒と溝の壁部と外気雰囲気の境界あたりで、微粒子の自己組織化現象を起こし得る状態となった微粒子懸濁液の溶媒の所定部分を意味している。ここでは、図1を参照して説明する。この図1には、基板の溝の壁部1に対する微粒子懸濁液2のメニスカス先端部の様子が表されている。微粒子懸濁液2の溶媒の膜厚が、微粒子2aによる粒子整列部厚み4をぎりぎり満たす程度にまで小さくなった部分(図中、「A」で示される。)から、溶媒と溝の壁部と外気雰囲気の境界の最先端までの部分(図中、「B」で示される。)では、乾燥7にともなう溶媒の流れ3と溶媒の表面張力とによって微粒子2aが個々に順次集合していく。この部分(図中、メニスカス先端部の長さ5で示される。)が「メニスカス先端部」である。そして乾燥7にともなって、この「メニスカス先端部」は、図中の下方に向かって後退6していき、基板の溝の壁部1の表面を移動していく。 In the method for producing a fine particle array structure of the present invention, the “meniscus tip” refers to the self-organization phenomenon of fine particles suspended in a solvent around the boundary between the solvent, the groove wall and the outside air. It means a predetermined portion of the solvent of the fine particle suspension that has become a state that can be caused. Here, it demonstrates with reference to FIG. FIG. 1 shows the state of the meniscus tip of the fine particle suspension 2 with respect to the wall 1 of the substrate groove. From the portion (indicated by “A” in the figure) where the film thickness of the solvent of the fine particle suspension 2 is reduced to the extent that the particle alignment portion thickness 4 due to the fine particles 2a is filled, the wall portion of the solvent and the groove. In the portion up to the front edge of the boundary between the atmosphere and the outside atmosphere (indicated by “B” in the figure), the fine particles 2 a are successively assembled individually by the solvent flow 3 accompanying the drying 7 and the surface tension of the solvent. . This portion (indicated by the length of the meniscus tip 5 in the figure) is the “meniscus tip”. With the drying 7, this “meniscus tip” retreats 6 downward in the figure and moves on the surface of the wall 1 of the substrate groove.
本発明の微粒子配列構造体の製造方法においては、上記メニスカス先端部が、前記溝の壁部の選択された所定の領域のみを移動するようにして、前記溝の選択された所定の壁部にのみ、前記微粒子の配列集合体を形成させることができる。 In the method for producing a fine particle array structure of the present invention, the meniscus tip is moved only in a selected predetermined region of the groove wall so as to move to the selected predetermined wall of the groove. Only an array aggregate of the fine particles can be formed.
本発明の微粒子配列構造体の製造方法においては、まず、表面に所定の幅及び深さを有する溝が形成された基板を準備する。溝が形成された基板の該溝の形成方法については、基板の材質や、得ようとする溝の構造等に適するものを適宜選択すればよく、特に制限はないが、例えば基板の材質がシリコンである場合には、深堀り反応性イオンエッチング(DRIE:Deep Reactive Ion Etching)で行うことができる。 In the method for producing a fine particle array structure according to the present invention, first, a substrate having a groove with a predetermined width and depth formed on the surface is prepared. A method for forming the groove of the substrate on which the groove is formed may be appropriately selected from materials suitable for the material of the substrate and the structure of the groove to be obtained, and is not particularly limited. For example, the material of the substrate is silicon. In this case, it can be performed by deep reactive ion etching (DRIE).
この深堀り反応性イオンエッチング(DRIE)について、図2を参照して説明すると、表面に所定の開口12部を設けて保護マスク11で覆った基板10に対し、六フッ化硫黄(SF6)などのプラズマイオンで垂直方向にエッチングを行う。そのエッチングによって形成した溝13の内壁面をテフロン系のガス(C4F8)などの保護膜14で保護する。このエッチングと保護膜形成の工程を繰り返すことで、前記保護マスクの開口部に溝13が形成される。エッチング工程の後の保護膜形成によって、溝13の底面にも保護膜14が形成されるが、次段階のエッチング工程において、六フッ化硫黄(SF6)のプラズマイオンが底面の保護膜14にアタックして除去しつつ垂直方向へのエッチングをすすめ、一方、横方向に対しては上記プラズマイオンの照射が弱いので、保護膜14は除去されずに側壁面がエッチングから保護される。 The deep reactive ion etching (DRIE) will be described with reference to FIG. 2. Sulfur hexafluoride (SF 6 ) is applied to the substrate 10 provided with a predetermined opening 12 on the surface and covered with the protective mask 11. Etch in the vertical direction with plasma ions such as. The inner wall surface of the groove 13 formed by the etching is protected by a protective film 14 such as a Teflon-based gas (C 4 F 8 ). By repeating this etching and protective film forming step, a groove 13 is formed in the opening of the protective mask. By forming the protective film after the etching process, the protective film 14 is also formed on the bottom surface of the groove 13. In the next etching process, plasma ions of sulfur hexafluoride (SF 6 ) are applied to the protective film 14 on the bottom surface. Etching in the vertical direction is recommended while removing by attack. On the other hand, since the plasma ion irradiation is weak in the lateral direction, the protective film 14 is not removed and the side wall surface is protected from etching.
図3aには、深堀り反応性イオンエッチング(DRIE)で得られた溝の顕微鏡写真の一例を示す。また、図3bにはその模式図を示す。溝の側壁面の形状が、一段毎に図正面から見て左右方向に窪んでいるスキャロップ形状と呼ばれる形状15になっているのは、プラズマに電界をかけて異方性を出してはいるが、化学反応に由来する横方向のエッチングが生じるためである。なお、図3に示す溝の側壁面のスキャロップ形状は、溝の深さ方向の長さ当たりの数がおよそ1個/μmであり、一段毎のくぼみの最大深さがおよそ500nmであるが、上記プラズマイオンの照射時間を調整することで、前者を0.1〜10個/μmの範囲で、後者を100〜1000nmの範囲で制御することが可能である。 FIG. 3a shows an example of a micrograph of a groove obtained by deep reactive ion etching (DRIE). FIG. 3b shows a schematic diagram thereof. The shape of the side wall surface of the groove is a shape 15 called a scallop shape that is recessed in the left-right direction when viewed from the front of the figure, although it causes anisotropy by applying an electric field to the plasma. This is because lateral etching resulting from a chemical reaction occurs. In addition, the scalloped shape of the side wall surface of the groove shown in FIG. 3 is about 1 piece / μm per length in the depth direction of the groove, and the maximum depth of the dent for each step is about 500 nm. By adjusting the plasma ion irradiation time, it is possible to control the former in the range of 0.1 to 10 / μm and the latter in the range of 100 to 1000 nm.
本発明の微粒子配列構造体の製造方法においては、また、微粒子を溶媒に懸濁してなる微粒子懸濁液を準備する。用いる溶媒としては、粘度、微粒子の分散性や、基板に対する濡れ性などによって、適宜に選択すればよいが、一般的には例えば、水、エタノール、イソプロピルアルコール(IPA)、キシレン、トルエンなどが例示できる。 In the method for producing a fine particle array structure of the present invention, a fine particle suspension obtained by suspending fine particles in a solvent is prepared. The solvent to be used may be appropriately selected depending on the viscosity, the dispersibility of the fine particles, the wettability with respect to the substrate, etc., but generally, for example, water, ethanol, isopropyl alcohol (IPA), xylene, toluene and the like are exemplified. it can.
本発明の微粒子配列構造体の製造方法においては、上記溝が形成された基板の該溝に、上記微粒子を溶媒に懸濁してなる微粒子懸濁液を充填する。微粒子懸濁液を充填する方法に特に制限はなく、その溝の上に噴霧、滴下するなどして載置し、毛細管現象により溝に上記微粒子懸濁液が充填させるなどして行うことができる。 In the method for producing a fine particle array structure of the present invention, a fine particle suspension obtained by suspending the fine particles in a solvent is filled in the grooves of the substrate on which the grooves are formed. There is no particular limitation on the method of filling the fine particle suspension, and the fine particle suspension can be placed by spraying, dropping, or the like on the groove and filling the groove with the fine particle suspension by capillary action. .
本発明の微粒子配列構造体の製造方法においては、上記溝に充填した微粒子縣濁液の溶媒を乾燥させる。乾燥の方法は、自然乾燥でもよく、溶媒の蒸発を促進させるために、減圧下に行ってもよい。 In the method for producing a fine particle array structure of the present invention, the solvent of the fine particle suspension filled in the groove is dried. The drying method may be natural drying or may be performed under reduced pressure in order to promote evaporation of the solvent.
ここで、図4を参照して、上記充填、乾燥の工程の好ましい態様の一例を説明する。ここでは、ビーカーを載せることができる支持台と、シリコン基板を保持して垂直方向に上下移動できるアームとを備えた基板の保持移動装置(図示せず)を用いる。微粒子懸濁液を入れた容器20を前記基板の保持移動装置の支持台(図示せず)に置く。他方で溝の形成されたシリコン基板10は、前記基板の保持移動装置のアーム(図示せず)に保持されている。シリコン基板を保持したままアームを下方に移動させて、基板の溝の少なくとも一部が微粒子懸濁液に接触するように浸漬させ、所定位置でアームを停止する。この状態で一定時間おくと微粒子縣濁液2は毛細管現象によって前記基板10の溝に充填する。次いで前記アームを上方に移動させて前記基板10を微粒子懸濁液2から引き上げて室内、又は温度、湿度、気圧等の制御された外気雰囲気下で乾燥させる。前記基板の保持移動装置を恒温室内に設置して上記操作を行うことで、温度、湿度、気圧等の制御された外気雰囲気下で乾燥させることが容易となる。 Here, with reference to FIG. 4, an example of the preferable aspect of the process of the said filling and drying is demonstrated. Here, a substrate holding / moving device (not shown) including a support table on which a beaker can be placed and an arm that holds the silicon substrate and can move vertically is used. The container 20 containing the fine particle suspension is placed on a support (not shown) of the substrate holding and moving device. On the other hand, the silicon substrate 10 in which the groove is formed is held by an arm (not shown) of the holding and moving device for the substrate. The arm is moved downward while holding the silicon substrate, so that at least a part of the groove of the substrate is in contact with the fine particle suspension, and the arm is stopped at a predetermined position. In this state, the fine particle suspension 2 is filled in the groove of the substrate 10 by capillary action. Next, the arm is moved upward to pull up the substrate 10 from the fine particle suspension 2 and dry it indoors or in an outside air atmosphere in which temperature, humidity, pressure, etc. are controlled. By performing the above operation by installing the substrate holding and moving device in a temperature-controlled room, it becomes easy to dry the substrate under a controlled outside air atmosphere such as temperature, humidity, and atmospheric pressure.
このとき、微粒子懸濁液の溝への均一な充填のためには、溝の長さ方向がシリコン基板を上下させる方向と同じ方向であることが好ましいが、それ以外の方向に形成されていてもよい。また、浸漬時間(アームを所定位置に停止させてから上方に移動させ始めるまでの時間)は例えば1〜30秒程度で行うことができ、引き上げ速度は例えば1μm〜20mm/秒程度で行うことができる。 At this time, in order to uniformly fill the grooves of the fine particle suspension, it is preferable that the length direction of the grooves is the same as the direction in which the silicon substrate is moved up and down, but the grooves are formed in other directions. Also good. In addition, the immersion time (the time from when the arm is stopped at a predetermined position to when it starts to move upward) can be performed in about 1 to 30 seconds, for example, and the lifting speed can be performed in about 1 μm to 20 mm / second, for example. it can.
本発明の微粒子配列構造体の製造方法においては、微粒子懸濁液の溶媒が乾燥するにつれて、上記メニスカス先端部が、前記溝の壁部の選択された所定の領域のみを移動するようにさせる。その態様としては例えば下記のようなものが挙げられる。 In the method for producing a fine particle array structure according to the present invention, as the solvent of the fine particle suspension is dried, the meniscus tip is moved only in a predetermined region of the groove wall. Examples of such an embodiment include the following.
(1)微粒子懸濁液における微粒子の溶媒に対する体積率を調整する。
すなわち後述の実施例で示されるように、ポリスチレンビーズを水に懸濁した微粒子懸濁液を、シリコン基板上に形成した幅50μm×深さ100μmの微細溝に充填して、室温で自然乾燥させると、まず、側壁面に上記メニスカス先端部が生じ、それが側壁面の一定の領域を移動する。したがって、上記メニスカス先端部が移動した領域で微粒子の配列集合体が形成され、微粒子懸濁液に含有せしめる微粒子を所定数量に制限しておけば、集合体を形成し得る微粒子が枯渇するので、枯渇した段階でそれ以外の側壁面や底面には微粒子の配列集合体は形成されない。
(1) The volume ratio of the fine particles in the fine particle suspension to the solvent is adjusted.
That is, as shown in the examples described later, a fine particle suspension in which polystyrene beads are suspended in water is filled in a fine groove having a width of 50 μm and a depth of 100 μm formed on a silicon substrate, and is naturally dried at room temperature. First, the meniscus tip is generated on the side wall surface, and it moves in a certain region of the side wall surface. Therefore, an array aggregate of fine particles is formed in the region where the meniscus tip moves, and if the number of fine particles to be contained in the fine particle suspension is limited to a predetermined number, the fine particles that can form the aggregate are depleted. At the stage of depletion, fine particle array aggregates are not formed on the other side wall surface and bottom surface.
(2)外気雰囲気における温度、湿度、及び/又は気圧を調整する。
すなわち後述の実施例で示されるように、外気雰囲気の湿度を下げて、上記メニスカス先端部の溶媒の乾燥速度を高めると、微粒子の自己組織化が促進される。したがって、外気雰囲気における温度、湿度、及び/又は気圧を調整して、乾燥速度を高めれば、その領域あたりの充填率が上がり、その充填率が上がるにつれ単層から複数層に微粒子が配列するようになる。一方で、上記(1)と同様に、微粒子懸濁液に含有せしめる微粒子を所定数量に制限しておけば、集合体を形成し得る微粒子が枯渇するので、枯渇した段階でそれ以外の側壁面や底面には微粒子の配列集合体は形成されない。したがって、その分、微粒子の配列集合体が形成される領域はより制限される。
(2) Adjust the temperature, humidity, and / or pressure in the outside air atmosphere.
That is, as shown in the examples described later, when the humidity of the outside air atmosphere is lowered and the drying speed of the solvent at the meniscus tip is increased, self-organization of the fine particles is promoted. Therefore, if the drying rate is increased by adjusting the temperature, humidity, and / or pressure in the outside air atmosphere, the filling rate per region increases, and as the filling rate increases, fine particles are arranged from a single layer to multiple layers. become. On the other hand, as in the above (1), if the number of fine particles to be contained in the fine particle suspension is limited to a predetermined number, the fine particles that can form an aggregate are depleted. No array of fine particles is formed on the bottom surface. Therefore, the region where the array aggregate of fine particles is formed is more limited accordingly.
(3)溝の壁部における溶媒に対する濡れ性を調整する。
微粒子の配列集合体を形成させる領域以外の壁部に対して、微粒子懸濁液の溶媒に対する濡れ性を調整して、その所定領域の壁部にメニスカス先端部が生じないようにすれば、所望の領域の壁部にのみ、前記微粒子の配列集合体を形成させることができる。
(3) Adjust the wettability of the groove wall to the solvent.
Desirable by adjusting the wettability of the fine particle suspension to the solvent on the wall portion other than the region where the fine particle array aggregate is formed so that the meniscus tip portion does not occur in the wall portion of the predetermined region. The array of fine particles can be formed only on the wall of the region.
すなわち後述の実施例で示されるように、例えば撥水被膜処理を施した壁部の水に対する濡れ性は非常に小さく、水は壁部に対する大きな接触角を保ったまま乾燥する。したがって、メニスカス先端部は生じずに微粒子の配列集合体が形成されることがない。 That is, as shown in the examples described later, for example, the water wettability of the wall portion subjected to the water repellent coating treatment is very small, and the water dries while maintaining a large contact angle with the wall portion. Therefore, the tip of the meniscus is not generated, and an array aggregate of fine particles is not formed.
そこで、例えば、上記に説明した深堀り反応性イオンエッチング(DRIE)において、溝側壁面の保護膜として、撥水被膜(フルオロカーボン膜)を施す。これにより、側壁での微粒子集合体の形成を妨げることができ、それ以外の領域(底面)での微粒子の配列集合体の形成を促すことができる。 Therefore, for example, in the deep reactive ion etching (DRIE) described above, a water-repellent coating (fluorocarbon film) is applied as a protective film on the groove sidewall surface. Thereby, formation of the fine particle aggregate on the side wall can be prevented, and formation of the fine particle array aggregate in the other region (bottom surface) can be promoted.
本発明の微粒子配列構造体の製造方法においては、下記数式(1)に基づいて設定した条件で、上記溝に充填した上記微粒子縣濁液の溶媒を乾燥させることで、上記溝の選択された所定の壁部に対する上記微粒子の充填率(ε)が所望の値となるように制御することができる。 In the method for producing the fine particle array structure of the present invention, the groove is selected by drying the solvent of the fine particle suspension filled in the groove under the conditions set based on the following mathematical formula (1). The filling rate (ε) of the fine particles with respect to the predetermined wall portion can be controlled to a desired value.
ここで、充填率[%]とは、単位体積あたりを占有する微粒子の体積のことである。メニスカス後退速度[m/s]とは、液体の体積減少に伴ったメニスカス先端部の後退速度(移動速度)のことである。粒子整列部厚み[m]とは堆積した粒子膜の厚みのことである。乾燥速度[g/m・s]とは溶媒の乾燥速度のことである。メニスカスの長さ[m]とはメニスカス先端部の長さのことである。微粒子の溶液に対する体積率[%]とは、用いる微粒子懸濁液中の微粒子の溶液に対する体積率のことである。これらのパラメータは電子顕微鏡などでの観察により実測することも可能である。なお、比例定数βは上記パラメータを相関付ける比例定数である。 Here, the filling rate [%] is the volume of fine particles occupying per unit volume. The meniscus retracting speed [m / s] is the retracting speed (moving speed) of the meniscus tip as the liquid volume decreases. The particle alignment portion thickness [m] is the thickness of the deposited particle film. The drying rate [g / m · s] is the drying rate of the solvent. The meniscus length [m] is the length of the meniscus tip. The volume ratio [%] with respect to the solution of fine particles is the volume ratio with respect to the solution of fine particles in the fine particle suspension to be used. These parameters can be actually measured by observation with an electron microscope or the like. The proportionality constant β is a proportionality constant that correlates the above parameters.
以下実施例を挙げて本発明を更に詳細に説明するが、これらの実施例は本発明の範囲を限定するものではない。 EXAMPLES Hereinafter, although an Example is given and this invention is demonstrated further in detail, these Examples do not limit the scope of the present invention.
<製造例1> (微粒子配列構造体の製造 その1)
表面に幅50μm×深さ100μm×長さ10mmのトレンチ状の溝が形成されたシリコン基板を、上記に説明した深堀り反応性イオンエッチング(DRIE)で得た。
<Production Example 1> (Production of Fine Particle Array Structure 1)
A silicon substrate having a trench-like groove of 50 μm width × 100 μm depth × 10 mm length formed on the surface was obtained by deep reactive ion etching (DRIE) as described above.
一方、ビーカーを載せることができる支持台と、シリコン基板を保持して垂直方向に上下移動できるアームとを備えた基板の保持移動装置を、恒温室に設置した。この基板の保持移動装置の脇にはCCD顕微鏡を配置し、上記トレンチ状の溝内部の様子を観察、記録できるようにした。 On the other hand, a substrate holding and moving device provided with a support table on which a beaker can be placed and an arm that can hold a silicon substrate and move vertically in the vertical direction was installed in a temperature-controlled room. A CCD microscope was placed beside the substrate holding and moving device so that the inside of the trench-like groove could be observed and recorded.
上記基板の保持移動装置の支持台に、ポリスチレンビーズ(Thermo Fisher Scientific 社製、粒径 1μm)の6体積%水懸濁液を入れた容器を置き、他方で上記トレンチ状の溝を有するシリコン基板を、基板の保持移動装置のアームに取り付けて、これを保持したままを下方に移動させて、基板の溝の少なくとも一部が微粒子懸濁液に接触するように浸漬させ、所定位置でアームを停止させた。この状態で5秒置き、5mm/秒でアームを上方に移動させて、上記基板を引き上げた。その基板をアームに取り付けたままの状態で、温度22℃湿度55%に保たれた恒温室内で10分間静置し、上記微粒子懸濁液の溶媒である水を乾燥させた。 A silicon substrate having a trench-like groove on the other hand, a container containing 6% by volume water suspension of polystyrene beads (manufactured by Thermo Fisher Scientific, particle size: 1 μm) placed on the support of the substrate holding and moving device. Is attached to the arm of the substrate holding and moving device, and is moved downward while holding the substrate so that at least a part of the groove of the substrate is in contact with the fine particle suspension. Stopped. In this state, the arm was moved upward at 5 mm / sec for 5 seconds, and the substrate was pulled up. With the substrate still attached to the arm, the substrate was allowed to stand for 10 minutes in a temperature-controlled room maintained at a temperature of 22 ° C. and a humidity of 55% to dry the water as the solvent for the fine particle suspension.
図5aには、得られた微粒子配列構造体の顕微鏡写真を示す。また、図5bには図5aに示す顕微鏡写真の部分拡大写真を示す。なお、図5cは得られた微粒子配列構造体を模式的に表した図である。これらの顕微鏡写真にみられるように、溝の内部の側壁に、スチレンビーズが規則正しく単層に配列した微粒子の配列集合体が形成していることがわかる。その一方で、溝の内部の底面には、スチレンビーズの配列集合体が形成していないことがわかる。 FIG. 5a shows a micrograph of the obtained fine particle array structure. FIG. 5b shows a partially enlarged photograph of the micrograph shown in FIG. 5a. FIG. 5c is a diagram schematically showing the obtained fine particle array structure. As can be seen from these micrographs, it can be seen that an array of fine particles in which styrene beads are regularly arranged in a single layer is formed on the side wall inside the groove. On the other hand, it can be seen that an array aggregate of styrene beads is not formed on the bottom surface inside the groove.
<製造例2> (微粒子配列構造体の製造 その2)
異なる粒径(0.5μm)のポリスチレンビーズ(Thermo Fisher Scientific 社製、粒径 0.5μm)を用い、温度25℃湿度40%に保たれた恒温室内で微粒子懸濁液の溶媒である水を乾燥させた以外は、製造例1と同様にして、微粒子配列構造体を得た。
<Production Example 2> (Production of Fine Particle Array Structure 2)
Using polystyrene beads of different particle sizes (0.5 μm) (Thermo Fisher Scientific, particle size 0.5 μm), water as a solvent of the fine particle suspension is dried in a temperature-controlled room maintained at a temperature of 25 ° C. and a humidity of 40%. Except for the above, a fine particle array structure was obtained in the same manner as in Production Example 1.
図6aには、得られた微粒子配列構造体の顕微鏡写真を示す。なお、図6bは得られた微粒子配列構造体を模式的に表した図である。これらの顕微鏡写真にみられるように、溝の内部の側壁に、スチレンビーズが規則正しく複層に配列した微粒子の配列集合体が形成していることがわかる。 FIG. 6a shows a micrograph of the obtained fine particle array structure. FIG. 6b is a diagram schematically showing the obtained fine particle array structure. As can be seen from these micrographs, it can be seen that an array of fine particles in which styrene beads are regularly arranged in multiple layers is formed on the side wall inside the groove.
<試験例1> (微粒子の選択的な領域への配列のメカニズムの考察 その1)
製造例1及び製造例2においては、いずれも微粒子の配列集合体が溝の内部の側壁に形成され、その底面には形成されなかった。そこで、この選択的な領域への配列のメカニズムについて検討した。
<Test Example 1> (Consideration of Mechanism of Arrangement of Fine Particles into Selective Regions 1)
In each of Production Example 1 and Production Example 2, an array aggregate of fine particles was formed on the side wall inside the groove, but not on the bottom surface. Therefore, the mechanism of the sequence to this selective region was examined.
そのために、上記製造例1及び製造例2と同じく、表面に幅50μm×深さ100μm×長さ10mmのトレンチ状の溝が形成されたシリコン基板を準備した。この基板の溝に純水を滴下して充填し、その純水の乾燥過程をCCD顕微鏡で観察した。 Therefore, a silicon substrate having a trench-like groove having a width of 50 μm, a depth of 100 μm and a length of 10 mm formed on the surface was prepared in the same manner as in Production Example 1 and Production Example 2 above. Pure water was dropped and filled into the groove of the substrate, and the drying process of the pure water was observed with a CCD microscope.
図7には、乾燥開始直後(a)、乾燥開始12秒後(b)、乾燥開始26秒後(c)、乾燥開始120秒後(d)の断面の顕微鏡写真を示す。また、この結果から考察される、微粒子の配列のメカニズムの模式的概略図を、図8a〜dに示す。 FIG. 7 shows micrographs of cross sections immediately after the start of drying (a), 12 seconds after the start of drying (b), 26 seconds after the start of drying (c), and 120 seconds after the start of drying (d). Moreover, the schematic schematic of the mechanism of the arrangement | sequence of microparticles | fine-particles considered from this result is shown to FIG.
図8a〜dに示すように、製造例1及び製造例2において溝の内部の側壁に選択的に微粒子の配列が起こるのは、その壁部には微粒子が懸濁した溶媒の溝の壁部に対するメニスカス先端部が生じるのに対して、底面には生じないからであると考えられた。 As shown in FIGS. 8a to 8d, in the production example 1 and the production example 2, the fine particles are selectively arranged on the side wall inside the groove. The wall portion of the groove of the solvent in which the fine particles are suspended is formed on the wall portion. It is thought that this is because a meniscus tip portion with respect to is not generated on the bottom surface.
このことを、図9を参照して更に説明すると、溝の内部の側壁においては、乾燥にともない、溶媒と溝の壁部と外気雰囲気の境界が後退(移動)し始める角度が充分に小さいために、微粒子が自己組織化するメニスカス先端部が生じ得ると考えられた(図9a)。これに対して、溝の内部の底面においては、乾燥にともない、溶媒と溝の壁部と外気雰囲気の境界が後退(移動)し始める角度が充分に小さくならないために、微粒子が自己組織化するメニスカス先端部が生じないと考えられた(図9b)。 This will be further described with reference to FIG. 9 because the angle at which the boundary between the solvent, the wall of the groove, and the outside air atmosphere starts to recede (move) with the drying on the side wall inside the groove is sufficiently small. It was thought that a meniscus tip where fine particles self-assembled could occur (FIG. 9a). On the other hand, at the bottom surface inside the groove, as the drying, the angle at which the boundary between the solvent, the wall of the groove and the outside atmosphere begins to recede (move) does not become sufficiently small, so that the fine particles self-assemble. It was thought that no meniscus tip was formed (FIG. 9b).
<試験例2> (微粒子の選択的な領域への配列のメカニズムの考察 その2)
上記メニスカス先端部に関わる状態パラメータと、単位体積あたりの微粒子の充填率(ε)については、下記数式(1)によって表すことができることが知られている(現代界面コロイド化学の基礎 平成14年5月15日 日本化学会 丸善株式会社)。
<Test Example 2> (Consideration of Mechanism of Arrangement of Fine Particles into Selective Region 2)
It is known that the state parameter related to the meniscus tip and the fine particle filling rate (ε) per unit volume can be expressed by the following formula (1) (Basics of Modern Interfacial Colloid Chemistry, May 2002) March 15 The Chemical Society of Japan Maruzen Co., Ltd.).
そこで、上記充填率を制御するために利用できる制御因子について検討した。その結果、粒子整列部厚みh[m]は、壁部の粗さ、溶媒の粘度、基板と溶媒の濡れ性、溶媒の表面張力、などで制御できると考えられた。また、メニスカス後退速度V[m/s]と乾燥速度Je[g/m・s]は、外気雰囲気の温度、湿度、気圧、などで制御できると考えられた。また、微粒子の溶液に対する体積率は、微粒子懸濁液の調整段階でこれを制御できると考えられた。 Then, the control factor which can be utilized in order to control the said filling rate was examined. As a result, it was considered that the particle alignment portion thickness h [m] can be controlled by wall roughness, solvent viscosity, substrate and solvent wettability, solvent surface tension, and the like. Further, it was considered that the meniscus receding speed V [m / s] and the drying speed Je [g / m · s] can be controlled by the temperature, humidity, atmospheric pressure, etc. of the outside air atmosphere. Further, it was considered that the volume ratio of the fine particles to the solution can be controlled in the fine particle suspension adjustment stage.
<試験例3> (微粒子の溶媒に対する体積率の影響)
微粒子懸濁液中の微粒子の溶媒に対する体積率が、上記微粒子の単位体積あたり充填率にどのような影響があるかを調べた。試験は、製造例1と同様にして、ポリスチレンビーズの配列集合体を形成させる際に、そのポリスチレンビーズの水に対する体積%を、0.03体積%、0.06体積%、0.12体積%、0.25体積%、0.5体積%、1体積%とかえて、微粒子配列構造体を製造し、その側壁に堆積した粒子を電子顕微鏡で観察し、その数を計測した。その結果を図10に示す。
<Test Example 3> (Effect of volume ratio of fine particles on solvent)
It was examined how the volume ratio of the fine particles in the fine particle suspension to the solvent affects the filling rate per unit volume of the fine particles. In the test, in the same manner as in Production Example 1, when an array assembly of polystyrene beads was formed, the volume percentage of the polystyrene beads with respect to water was 0.03 vol%, 0.06 vol%, 0.12 vol%, 0.25 vol%, 0.5 The fine particle array structure was manufactured in place of volume% and 1 volume%, and the particles deposited on the side wall were observed with an electron microscope and the number thereof was measured. The result is shown in FIG.
図10に明らかなように、微粒子懸濁液中の微粒子の溶媒に対する体積%を0〜1体積%の範囲でかえると、その範囲において、上記数式1から予測されたとおり、微粒子の充填率との間に正の相関が認められた。したがって、微粒子懸濁液中の微粒子の溶媒に対する体積率を調整することで、溝の内部の側壁における上記微粒子の単位体積あたり充填率を制御できることが明らかとなった。 As is clear from FIG. 10, when the volume% of the fine particles in the fine particle suspension is changed within the range of 0 to 1% by volume, the fine particle filling rate is A positive correlation was observed between the two. Therefore, it became clear that the filling rate per unit volume of the fine particles on the side wall inside the groove can be controlled by adjusting the volume ratio of the fine particles in the fine particle suspension to the solvent.
<試験例4> (外気雰囲気の湿度の影響)
外気雰囲気の湿度が、上記微粒子の単位体積あたり充填率にどのような影響があるかを調べた。試験は、製造例1と同様にして、ポリスチレンビーズの配列集合体を形成させる際に、その恒温室の室内の湿度を50、67、90%とかえて、微粒子配列構造体を製造し、その側壁に堆積した粒子をCCD顕微鏡で観察した。その結果を図11―図13に示す。
<Test Example 4> (Influence of humidity in the outside atmosphere)
The influence of the humidity of the outside atmosphere on the filling rate per unit volume of the fine particles was examined. In the test, in the same manner as in Production Example 1, when forming an array assembly of polystyrene beads, the humidity inside the temperature-controlled room was changed to 50, 67, and 90%, and a fine particle array structure was manufactured, and its side wall The particles deposited on were observed with a CCD microscope. The results are shown in FIGS.
図11a,bに示すように、湿度50%で乾燥させると、側壁に単層の微粒子の配列集合体が形成されたのに対して、底面には微粒子がまばらに存在しているのみであって、微粒子の配列集合体は形成されなかった。なお、図11c,dは得られた顕微鏡写真を模式的に表した図である。 As shown in FIGS. 11a and 11b, when dried at a humidity of 50%, a single-layered array of fine particles was formed on the side wall, whereas only fine particles were present on the bottom surface. As a result, an array aggregate of fine particles was not formed. 11c and 11d are diagrams schematically showing the obtained micrographs.
図12a,bに示すように、湿度67%で乾燥させると、側壁に単層の微粒子の配列集合体が形成された。また、底面には微粒子がまばらに存在している部分と、それらが集合している部分が混在していた。なお、図12c,dは得られた顕微鏡写真を模式的に表した図である。 As shown in FIGS. 12a and 12b, when the film was dried at a humidity of 67%, a single-layer array of fine particles was formed on the side wall. Moreover, the part which microparticles | fine-particles existed sparsely and the part which those aggregated were mixed on the bottom face. 12c and 12d are diagrams schematically showing the obtained micrographs.
図13a,bに示すように、湿度90%で乾燥させると、側壁に単層の微粒子の配列集合体が形成された。また、底面にも微粒子の配列集合体が形成された。なお、図13c,dは得られた顕微鏡写真を模式的に表した図である。 As shown in FIGS. 13a and 13b, when the film was dried at a humidity of 90%, an array of fine particle arrays was formed on the side wall. Also, an array of fine particles was formed on the bottom surface. FIGS. 13c and 13d are diagrams schematically showing the obtained micrographs.
以上から、外気雰囲気の湿度を調整することで、溝の内部の底面における上記微粒子の単位体積あたり充填率を制御できることが明らかとなった。 From the above, it became clear that the filling rate per unit volume of the fine particles on the bottom surface inside the groove can be controlled by adjusting the humidity of the outside air atmosphere.
<試験例5> (溝の壁部における溶媒に対する濡れ性の影響についての考察)
図14aには、フルオロカーボン膜処理したシリコン基板に水を滴下したときの状態を示す写真を示す。図14bには、硫酸/過酸化水素水混合溶液(SPM:Sulfuric acid /hydrogen Peroxide Mixture)で処理したシリコン基板に水を滴下したときの状態を示す写真を示す。図14aに示されるように、処理したシリコン基板に水を滴下した場合(図14b)に比べて、フルオロカーボン膜処理したシリコン基板表面における水の濡れ性は低く、水と基板との接触角は110度程度となった。したがって、溝の壁部の選択された所定の領域に、このような濡れ性を低下させる処理を施せば、上記メニスカス先端部が生じないため、部粒子の配列集合体の形成が起こらないものとないものと考えられた。
<Test Example 5> (Consideration of influence of wettability to solvent on groove wall)
FIG. 14a shows a photograph showing a state when water is dropped on a silicon substrate treated with a fluorocarbon film. FIG. 14 b shows a photograph showing a state when water is dropped onto a silicon substrate treated with a sulfuric acid / hydrogen peroxide mixture solution (SPM). As shown in FIG. 14a, the wettability of water on the surface of the silicon substrate treated with the fluorocarbon film is lower than when water is dropped on the treated silicon substrate (FIG. 14b), and the contact angle between water and the substrate is 110. It was about degrees. Therefore, if such a treatment for reducing wettability is performed on a selected predetermined region of the wall portion of the groove, the above-mentioned meniscus tip portion does not occur, so that the formation of an array aggregate of partial particles does not occur. I thought it was not.
1 基板の溝の壁部
2 微粒子懸濁液
2a 微粒子
3 溶媒の流れ
4 粒子整列部厚み
5 メニスカス先端部の長さ
6 メニスカス先端部の後退(移動)
7 液体の乾燥
10 シリコン基板
11 保護マスク
12 レジスト開口部
13 溝
14 保護膜
15 スキャロップ形状
20 容器
21 恒温室
22 引き上げ
30 ポリスチレンビーズの単層配列集合体
31 ポリスチレンビーズの複層配列集合体
32 微粒子の配列集合体
50 接触角
51 溶媒
66 基板/溶媒/外気の3者境界界面における溶媒の後退(移動)
DESCRIPTION OF SYMBOLS 1 Substrate groove wall 2 Fine particle suspension 2a Fine particle 3 Solvent flow 4 Particle alignment portion thickness 5 Meniscus tip length 6 Retraction (movement) of meniscus tip
7 Drying of liquid 10 Silicon substrate 11 Protective mask 12 Resist opening 13 Groove 14 Protective film 15 Scalloped shape 20 Container 21 Temperature-controlled room 22 Lifting 30 Polystyrene bead single layer array aggregate 31 Polystyrene bead multi-layer array aggregate 32 Array assembly 50 Contact angle 51 Solvent 66 Retraction (movement) of the solvent at the substrate / solvent / outside air interface
Claims (9)
(上記式中、Vはメニスカス後退速度[m/s]、hは粒子整列部厚み[m]、Jeは乾燥速度[g/m・s]、lはメニスカスの長さ[m]、φは微粒子の溶液に対する体積率[%]、βは比例定数、εは充填率[%]である。) Suspension of the fine particles filled in the groove under the conditions set based on the following formula (1) so that the filling rate (ε) of the fine particles with respect to the selected predetermined wall portion of the groove becomes a desired value. The method for producing a fine particle array structure according to any one of claims 1 to 8 , wherein the solvent of the liquid is dried.
(In the above formula, V is the meniscus retraction rate [m / s], h is the particle alignment portion thickness [m], Je is the drying rate [g / m · s], l is the meniscus length [m], and φ is (The volume fraction [%] of the fine particles in the solution, β is a proportional constant, and ε is the filling rate [%].)
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2009209244A JP5518406B2 (en) | 2009-09-10 | 2009-09-10 | Method for producing fine particle array structure |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2009209244A JP5518406B2 (en) | 2009-09-10 | 2009-09-10 | Method for producing fine particle array structure |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JP2011056626A JP2011056626A (en) | 2011-03-24 |
| JP5518406B2 true JP5518406B2 (en) | 2014-06-11 |
Family
ID=43944878
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP2009209244A Expired - Fee Related JP5518406B2 (en) | 2009-09-10 | 2009-09-10 | Method for producing fine particle array structure |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JP5518406B2 (en) |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105968893B (en) * | 2016-06-03 | 2019-01-01 | 东莞市交通规划勘察设计院有限公司 | A kind of pre-buried mounting base process of surface treatment of bridge cushion |
Family Cites Families (10)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2828386B2 (en) * | 1993-08-31 | 1998-11-25 | 科学技術振興事業団 | Manufacturing method of fine particle thin film |
| JP2003025300A (en) * | 2001-07-12 | 2003-01-29 | Fuji Photo Film Co Ltd | Method of introducing nano particle into micro space, and structure manufactured using it |
| JP2004117455A (en) * | 2002-09-24 | 2004-04-15 | Ricoh Co Ltd | Apparatus and method for producing fine-particle artificial crystal |
| JP4229812B2 (en) * | 2003-11-14 | 2009-02-25 | 株式会社リコー | Method for producing thin-film three-dimensional fine particle structure |
| JP4542770B2 (en) * | 2003-12-02 | 2010-09-15 | 宇部日東化成株式会社 | Manufacturing method of fine particle arrangement substrate and fine particle arrangement substrate obtained by the method |
| JP4249094B2 (en) * | 2004-06-16 | 2009-04-02 | 株式会社リコー | Method for manufacturing thin-film particulate assembly |
| JP2006035129A (en) * | 2004-07-28 | 2006-02-09 | Sony Corp | Fine particle array method, screen and device |
| JP2006291303A (en) * | 2005-04-12 | 2006-10-26 | Kyoto Univ | Fine particle assembly structure and its assembly method |
| WO2007060989A1 (en) * | 2005-11-22 | 2007-05-31 | Intellectual Property Bank Corp. | Method and apparatus for detecting trace substances by surface-enhanced raman scattering (sers), and microchannel chip for detection of microanalyte |
| KR20070113762A (en) * | 2006-05-26 | 2007-11-29 | 삼성전자주식회사 | Nanoparticle array method using capillary force and nanoparticle array produced by the same |
-
2009
- 2009-09-10 JP JP2009209244A patent/JP5518406B2/en not_active Expired - Fee Related
Also Published As
| Publication number | Publication date |
|---|---|
| JP2011056626A (en) | 2011-03-24 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| Li et al. | Physical processes-aided periodic micro/nanostructured arrays by colloidal template technique: fabrication and applications | |
| Zayer et al. | Accurate controlled deposition of silver nanoparticles on porous silicon by drifted ions in electrolytic solution | |
| Chen et al. | Applications of silicon nanowires functionalized with palladium nanoparticles in hydrogen sensors | |
| CN102781815B (en) | Conical nanostructures on substrate surfaces, in particular optical elements, methods for the production thereof and use thereof | |
| Diao et al. | Enhanced sensing performance and mechanism of CuO nanoparticle-loaded ZnO nanowires: Comparison with ZnO-CuO core-shell nanowires | |
| Yu et al. | Resistive switching behavior in memristors with TiO2 nanorod arrays of different dimensions | |
| CN110057869A (en) | A kind of semiconductor gas sensor and preparation method thereof | |
| JP2011523902A (en) | Process for manufacturing nanowire arrays | |
| US10079322B2 (en) | Necklaces of silicon nanowires | |
| CN103424441B (en) | Connectivity-adjustable palladium-based hydrogen sensor prepared on flexibility-controllable substrate and manufacturing method thereof | |
| Alwan et al. | High sensitivity and fast response at the room temperature of SnO2: CuO/PSi nanostructures sandwich configuration NH3 gas sensor | |
| EP2932526A1 (en) | Fabrication of three-dimensional high surface area electrodes | |
| Huang et al. | Pt surface modification of SnO 2 nanorod arrays for CO and H 2 sensors | |
| CN103451632A (en) | Micro-nano silver, copper or silver-copper alloy film and preparation method thereof | |
| Jones et al. | Photo-reduction of silver salts on highly heterogeneous lead zirconate titanate | |
| Chen et al. | Silicon carbide nano-via arrays fabricated by double-sided metal-assisted photochemical etching | |
| Yan et al. | Electrodeposited tungsten oxide films onto porous silicon for NO2 detection at room temperature | |
| CN108227057A (en) | A kind of SERS substrates based on grating resonance and preparation method thereof | |
| CN105866187B (en) | Semiconductor gas sensor and preparation method thereof | |
| CN100557083C (en) | A kind of implantable ultra-thin nanoporous gold membrane and its preparation method | |
| CN103030097B (en) | Method for preparing wafer level low-dimensional nanostructures based on electrostatic field self-focusing | |
| Brodoceanu et al. | Fabrication of metal nanoparticle arrays by controlled decomposition of polymer particles | |
| JP5518406B2 (en) | Method for producing fine particle array structure | |
| Shklovsky et al. | Bioinspired peptide nanotubes: Deposition technology and physical properties | |
| Dong et al. | Facile synthesis of CuO micro-sheets over Cu foil in oxalic acid solution and their sensing properties towards n-butanol |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| A711 | Notification of change in applicant |
Free format text: JAPANESE INTERMEDIATE CODE: A712 Effective date: 20110422 |
|
| A621 | Written request for application examination |
Free format text: JAPANESE INTERMEDIATE CODE: A621 Effective date: 20120907 |
|
| A711 | Notification of change in applicant |
Free format text: JAPANESE INTERMEDIATE CODE: A711 Effective date: 20121011 |
|
| RD04 | Notification of resignation of power of attorney |
Free format text: JAPANESE INTERMEDIATE CODE: A7424 Effective date: 20121016 |
|
| RD02 | Notification of acceptance of power of attorney |
Free format text: JAPANESE INTERMEDIATE CODE: A7422 Effective date: 20121022 |
|
| A521 | Request for written amendment filed |
Free format text: JAPANESE INTERMEDIATE CODE: A821 Effective date: 20121011 |
|
| A521 | Request for written amendment filed |
Free format text: JAPANESE INTERMEDIATE CODE: A821 Effective date: 20121022 |
|
| A711 | Notification of change in applicant |
Free format text: JAPANESE INTERMEDIATE CODE: A711 Effective date: 20130411 |
|
| RD04 | Notification of resignation of power of attorney |
Free format text: JAPANESE INTERMEDIATE CODE: A7424 Effective date: 20130411 |
|
| A521 | Request for written amendment filed |
Free format text: JAPANESE INTERMEDIATE CODE: A821 Effective date: 20130411 |
|
| A131 | Notification of reasons for refusal |
Free format text: JAPANESE INTERMEDIATE CODE: A131 Effective date: 20131217 |
|
| A521 | Request for written amendment filed |
Free format text: JAPANESE INTERMEDIATE CODE: A523 Effective date: 20140210 |
|
| TRDD | Decision of grant or rejection written | ||
| A01 | Written decision to grant a patent or to grant a registration (utility model) |
Free format text: JAPANESE INTERMEDIATE CODE: A01 Effective date: 20140401 |
|
| A61 | First payment of annual fees (during grant procedure) |
Free format text: JAPANESE INTERMEDIATE CODE: A61 Effective date: 20140402 |
|
| R150 | Certificate of patent or registration of utility model |
Ref document number: 5518406 Country of ref document: JP Free format text: JAPANESE INTERMEDIATE CODE: R150 |
|
| R250 | Receipt of annual fees |
Free format text: JAPANESE INTERMEDIATE CODE: R250 |
|
| R250 | Receipt of annual fees |
Free format text: JAPANESE INTERMEDIATE CODE: R250 |
|
| R250 | Receipt of annual fees |
Free format text: JAPANESE INTERMEDIATE CODE: R250 |
|
| R250 | Receipt of annual fees |
Free format text: JAPANESE INTERMEDIATE CODE: R250 |
|
| R250 | Receipt of annual fees |
Free format text: JAPANESE INTERMEDIATE CODE: R250 |
|
| R250 | Receipt of annual fees |
Free format text: JAPANESE INTERMEDIATE CODE: R250 |
|
| LAPS | Cancellation because of no payment of annual fees |