JPH10158012A - Production of porous silicon dioxide film - Google Patents

Production of porous silicon dioxide film

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Publication number
JPH10158012A
JPH10158012A JP31366896A JP31366896A JPH10158012A JP H10158012 A JPH10158012 A JP H10158012A JP 31366896 A JP31366896 A JP 31366896A JP 31366896 A JP31366896 A JP 31366896A JP H10158012 A JPH10158012 A JP H10158012A
Authority
JP
Japan
Prior art keywords
solvent
polymer
org
alkoxysilane
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.)
Granted
Application number
JP31366896A
Other languages
Japanese (ja)
Other versions
JP3851393B2 (en
Inventor
Takaaki Ioka
崇明 井岡
Tsuneaki Tanabe
恒彰 田辺
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.)
Asahi Chemical Industry Co Ltd
Original Assignee
Asahi Chemical Industry Co Ltd
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Filing date
Publication date
Application filed by Asahi Chemical Industry Co Ltd filed Critical Asahi Chemical Industry Co Ltd
Priority to JP31366896A priority Critical patent/JP3851393B2/en
Publication of JPH10158012A publication Critical patent/JPH10158012A/en
Application granted granted Critical
Publication of JP3851393B2 publication Critical patent/JP3851393B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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  • Formation Of Insulating Films (AREA)

Abstract

PROBLEM TO BE SOLVED: To obtain a uniform porous silicon dioxide film free from the formation of coarse grains by dissolving alkoxysilane and an amido bond-contg. org. polymer in a solvent, adding an acid, carrying out partial hydrolysis, adding a base, filmily coating the top of a substrate with the resultant soln., carrying out hydrolysis and dehydration condensation, removing the solvent and then removing the org. polymer from the resultant dry gel. SOLUTION: Alkoxysilane and an amido bond-contg. org. polymer such as poly(N-vinylcaprolactone) or a polyurethane deriv. are dissolved in a solvent, an acid is added and partial hydrolysis is carried out. A base catalyst is further added, the top of a substrate is filmily coated with the resultant soln. and hydrolysis and dehydration condensation are carried out. The solvent is evaporated and the org. polymer is removed from the resultant dry gel to obtain the objective porous silicon dioxide film. The org. polymer is removed from the dry gel film by firing by heating, solvent extraction or other method but it is easily removed by heating at a temp. above the thermal decomposition temp. of the polymer for about 1-24hr.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】本発明は、多孔質ケイ素酸化
物膜の製造方法に関する。
[0001] The present invention relates to a method for producing a porous silicon oxide film.

【0002】[0002]

【従来の技術】従来、LSI多層配線に用いる層間絶縁
膜には、ケイ素酸化物、またはフッ素や有機基を導入し
たケイ素酸化物が用いられてきた。しかしながら、これ
らの材料の比誘電率の値は比較的大きく、LSIの配線
が今後微細化されるに従って、これらの材料を層間絶縁
膜として用いることにより配線遅延などの諸問題が生ず
る。そのため、ケイ素酸化物を多孔化して、比誘電率の
値がおよそ1である空気との複合体にして比誘電率を低
下させるという試みがなされているが、いずれも複雑な
工程を含むため、良質なケイ素酸化物膜の簡便な製造方
法は確立されていない。
2. Description of the Related Art Conventionally, a silicon oxide or a silicon oxide into which fluorine or an organic group is introduced has been used for an interlayer insulating film used for an LSI multilayer wiring. However, the relative permittivity of these materials is relatively large, and as LSI wiring becomes finer in the future, the use of these materials as interlayer insulating films causes various problems such as wiring delay. For this reason, attempts have been made to make the silicon oxide porous and to reduce the relative permittivity by forming a composite with air having a relative permittivity of about 1, but all of them involve a complicated process. A simple method for producing a high-quality silicon oxide film has not been established.

【0003】三枝らの報告(Journal of M
acromolecular Science−Che
mistry,A27巻,13−14合併号 P.16
03−1612(1990)によると、アミド結合を含
むポリマーの存在下で酸触媒を用いてテトラアルコキシ
シランの加水分解、脱水縮合反応を行った場合、生成し
たケイ素酸化物ゲル中では、アミド結合のカルボニル基
とケイ素上のシラノール基とが水素結合して、分子レベ
ルで安定に分散しており、従ってその有機ポリマー分を
焼失させると、分子レベルの非常に小さな空孔が均一に
分散している多孔質ケイ素酸化物が得られる。
A report by Saegusa et al. (Journal of M)
acromolecular Science-Che
mystry, A27, 13-14 Merger No. 16
According to 03-1612 (1990), when the hydrolysis and dehydration condensation reaction of tetraalkoxysilane is performed using an acid catalyst in the presence of a polymer containing an amide bond, the amide bond of the generated silicon oxide gel is The carbonyl group and the silanol group on silicon are hydrogen-bonded and are stably dispersed at the molecular level. Therefore, when the organic polymer component is burned off, very small pores at the molecular level are uniformly dispersed. A porous silicon oxide is obtained.

【0004】しかしながら、上記報告に記載の方法で
は、加水分解、脱水縮合に要する時間が長く、ゲルの形
状が膜である場合には溶媒の蒸発が優先して起こるた
め、良質な膜を得ることができなかった。
[0004] However, in the method described in the above report, the time required for hydrolysis and dehydration condensation is long, and when the gel is a film, evaporation of the solvent takes precedence. Could not.

【0005】[0005]

【発明が解決しようとする課題】本発明は、巨大粒子の
生成などのない、均一で良質な多孔質ケイ素酸化物膜を
簡便かつ速やかに製造する方法を提供することを目的と
する。
SUMMARY OF THE INVENTION An object of the present invention is to provide a method for easily and quickly producing a uniform and high-quality porous silicon oxide film without generation of giant particles.

【0006】[0006]

【課題を解決するための手段】本発明は、アルコキシシ
ランと、アミド結合を含有する有機ポリマーを溶媒に溶
解し、酸を添加して部分的に加水分解した後、塩基触媒
を添加して基板上に膜状に塗布し加水分解、脱水縮合を
行い、その後に溶媒を蒸発させて得られた乾燥ゲルから
有機ポリマーを除去することを特徴とする多孔質ケイ素
酸化物膜の製造方法である。
According to the present invention, there is provided a method of dissolving an alkoxysilane and an organic polymer containing an amide bond in a solvent, adding an acid, partially hydrolyzing the solution, and then adding a base catalyst to the substrate. This is a method for producing a porous silicon oxide film, which comprises applying a film thereon, performing hydrolysis and dehydration condensation, and then removing an organic polymer from a dried gel obtained by evaporating a solvent.

【0007】以下、本発明を詳細に説明する。本発明の
多孔質ケイ素酸化物膜の製造法では、まずアミド結合を
含む有機ポリマーとアルコキシシランとを溶媒に溶解
し、触媒である酸と水を添加して撹拌することによっ
て、部分的に加水分解する工程を実施する。これにより
アルコキシシランは、部分的にケイ素水酸化物となり、
一部脱水縮合反応を起こすが、直ちにゲル化することは
ない。
Hereinafter, the present invention will be described in detail. In the method for producing a porous silicon oxide film of the present invention, first, an organic polymer containing an amide bond and an alkoxysilane are dissolved in a solvent, and an acid and water as a catalyst are added and stirred to partially hydrolyze. Perform a decomposition step. As a result, the alkoxysilane partially becomes a silicon hydroxide,
Although a partial dehydration reaction occurs, it does not gel immediately.

【0008】本発明において用いられるアルコキシシラ
ンの具体例としては、テトラメトキシシラン、テトラエ
トキシシラン、テトラ(i−プロピル)シラン、テトラ
(t−ブチル)シランなどのテトラアルコキシシラン、
およびこれらの混合物が挙げられる。また、上記のテト
ラアルコキシシランの部分加水分解物も用いることがで
きる。さらに多孔質膜を改良するために、ケイ素原子上
に1個のアルキル基やアリール基をもつアルコキシシラ
ンを用いたり、ケイ素原子上に1〜3個のアルキル基や
アリール基をもつアルコキシシランを上記のテトラアル
コキシシランに混合することも可能である。
[0008] Specific examples of the alkoxysilane used in the present invention include tetraalkoxysilanes such as tetramethoxysilane, tetraethoxysilane, tetra (i-propyl) silane and tetra (t-butyl) silane.
And mixtures thereof. Further, a partial hydrolyzate of the above tetraalkoxysilane can also be used. In order to further improve the porous film, an alkoxysilane having one alkyl group or an aryl group on a silicon atom or an alkoxysilane having one to three alkyl groups or an aryl group on a silicon atom is used. It is also possible to mix with tetraalkoxysilane.

【0009】本発明で用いられるアミド結合を含有する
有機ポリマーの具体例としては、ポリ(N−ビニルピロ
リドン)、ポリ(N−ビニルカプロラクトン)、ポリア
クリルアミド誘導体、ポリメタクリルアミド誘導体、ポ
リオキサゾリン誘導体、ポリイミド誘導体、ポリウレタ
ン誘導体、ポリ尿素誘導体、ナイロン誘導体およびこれ
らの混合物などが挙げられる。またこれらのポリマーの
構成成分であるモノマー同士の共重合体や、他の任意の
モノマーとの共重合体を用いてもよい。ポリマー中のア
ミド結合は、アルコキシシランのゲル化が起こる課程で
アルコキシシランが加水分解されて生成したシラノール
基と有効に水素結合して相分離を防止する。そのために
ポリマー中のアミド結合含有量は、アミド残基あたりの
分子量が5000以下であることが必要である。
Specific examples of the organic polymer containing an amide bond used in the present invention include poly (N-vinylpyrrolidone), poly (N-vinylcaprolactone), polyacrylamide derivative, polymethacrylamide derivative, polyoxazoline derivative, Examples include polyimide derivatives, polyurethane derivatives, polyurea derivatives, nylon derivatives, and mixtures thereof. Further, a copolymer of monomers which are constituent components of these polymers or a copolymer with any other monomer may be used. The amide bond in the polymer effectively forms a hydrogen bond with a silanol group generated by hydrolysis of the alkoxysilane during the process of gelation of the alkoxysilane, thereby preventing phase separation. For this purpose, the amide bond content in the polymer needs to be 5000 or less in molecular weight per amide residue.

【0010】これらのアミド結合含有有機ポリマーの添
加量は、アルコキシシラン100重量部に対し1〜10
000重量部、好ましくは10〜1000重量部であ
る。本発明で得られる多孔質膜の空隙率は主にアミド結
合含有有機ポリマーの添加量で決まる。したがってアミ
ド結合含有有機ポリマーの添加量が1重量部より少ない
と、空隙率が小さく多孔質膜の特性が現れない。また1
0000重量部より多いと、得られる多孔質膜の強度が
小さくなり実用性に乏しい。
The amount of the amide bond-containing organic polymer is from 1 to 10 parts by weight per 100 parts by weight of the alkoxysilane.
000 parts by weight, preferably 10 to 1000 parts by weight. The porosity of the porous film obtained by the present invention is mainly determined by the amount of the amide bond-containing organic polymer. Therefore, if the amount of the amide bond-containing organic polymer is less than 1 part by weight, the porosity is small and the characteristics of the porous film do not appear. Also one
If the amount is more than 0000 parts by weight, the strength of the obtained porous membrane becomes small, and the practicability is poor.

【0011】溶媒としては、用いているアルコキシシラ
ンとアミド結合含有有機ポリマーの両方が溶解する溶媒
であることが好ましく、C1〜C4の一価アルコール、
ジメチルホルムアミド、ホルムアミド、ジメチルアセト
アミドなどが好適に用いられる。これらの溶媒を混合し
たり、他の任意の溶媒あるいは添加物を混合してもよ
い。
The solvent is preferably a solvent in which both the alkoxysilane and the amide bond-containing organic polymer are dissolved, and a monohydric alcohol of C1 to C4,
Dimethylformamide, formamide, dimethylacetamide and the like are preferably used. These solvents may be mixed, or any other solvent or additive may be mixed.

【0012】触媒である酸の具体例としては塩酸、硝
酸、硫酸、酢酸などが挙げられる。これらの酸の添加量
はアルコキシシラン1モルに対し10-5〜1モル、好ま
しくは10-4〜10-1モルが適当である。触媒の添加量
が10-5モルより少ないと加水分解が十分に進まず、次
の工程でゲル化が起こらない場合がある。また、1モル
より多いと沈殿の生成などが起こり均一な多孔質膜が得
られなかったり、次の工程を実施する前にゲル化してし
まったりする。
Specific examples of the acid serving as a catalyst include hydrochloric acid, nitric acid, sulfuric acid, and acetic acid. The addition amount of these acids is 10 -5 to 1 mol, preferably 10 -4 to 10 -1 mol, per 1 mol of the alkoxysilane. If the amount of the catalyst is less than 10 -5 mol, hydrolysis does not proceed sufficiently and gelation may not occur in the next step. On the other hand, if it is more than 1 mol, precipitation or the like occurs, and a uniform porous film cannot be obtained, or gelation occurs before the next step is performed.

【0013】この工程で起こるアルコキシシランの加水
分解は、これら触媒である酸が水溶液である場合にはそ
の溶媒である水によって起こるし、必要ならば別途水を
添加する。適当な水の量は原料のアルコキシシランの種
類にもよるが、アルコキシシラン1モルに対し0.3〜
100モル、好ましくは1〜10モルである。0.3モ
ルより少ないと加水分解が十分に進まず、次の工程で速
やかにゲル化しないため、良質な膜を得ることができな
い。また100モルより多いと多孔質膜の均質性が低下
する。
[0013] The hydrolysis of the alkoxysilane which occurs in this step is caused by water as a solvent when the acid serving as the catalyst is an aqueous solution, and if necessary, water is added separately. The appropriate amount of water depends on the type of the alkoxysilane as a raw material, but is preferably from 0.3 to 1 mol per mol of the alkoxysilane.
It is 100 moles, preferably 1 to 10 moles. If the amount is less than 0.3 mol, hydrolysis does not proceed sufficiently, and gelation does not occur rapidly in the next step, so that a high quality film cannot be obtained. If the amount is more than 100 mol, the uniformity of the porous film is reduced.

【0014】酸触媒を用いた部分加水分解反応の温度は
0〜100℃、好ましくは20〜60℃である。0℃未
満では反応速度が小さく、加水分解を十分に進行させる
のに長時間を要し、また100℃を超える温度では次の
工程を実施する前にゲル化する場合がある。ゲル化に要
する時間はゲル化の温度や触媒の量などによって異なる
が、通常数時間〜数日間の範囲である。
[0014] The temperature of the partial hydrolysis reaction using an acid catalyst is 0 to 100 ° C, preferably 20 to 60 ° C. If the temperature is lower than 0 ° C., the reaction rate is low, and it takes a long time for hydrolysis to proceed sufficiently. If the temperature exceeds 100 ° C., gelation may occur before the next step is performed. The time required for gelling varies depending on the gelling temperature, the amount of catalyst, and the like, but is usually in the range of several hours to several days.

【0015】本発明の多孔質ケイ素酸化物膜の製造法で
は、上記の方法で得られたアルコキシシランの部分加水
分解物の溶液に、触媒である塩基および必要に応じて水
を添加し、基板上に膜状塗布した後にアルコキシシラン
の加水分解、脱水縮合を終了させる。ここで用いる塩基
の具体例としてはアンモニア水、水酸化カリウム、水酸
化ナトリウム、トリエチルアミン、トリエタノールアミ
ンなどが挙げられる。これらの塩基は、前の工程で加え
た酸よりもある程度過剰に加えることが重要であり、塩
基の添加量があまり少ないとゲル化しなかったり、ゲル
化に長時間を要するため、良質な膜が得られない。塩基
の添加量は原料のアルコキシシラン1モルに対し、前の
工程で添加した酸よりも10-5〜1モル、好ましくは1
-4〜10-1モル過剰とするのが適当である。塩基の過
剰量が1モルより多いと急激な粘度上昇が起こり膜状塗
布が困難になったり、瞬時にゲル化してしまったりす
る。
In the method for producing a porous silicon oxide film of the present invention, a base as a catalyst and, if necessary, water are added to a solution of the partial hydrolyzate of alkoxysilane obtained by the above method, After being coated on the film, hydrolysis and dehydration condensation of the alkoxysilane are terminated. Specific examples of the base used here include aqueous ammonia, potassium hydroxide, sodium hydroxide, triethylamine, and triethanolamine. It is important that these bases are added to some extent in excess of the acid added in the previous step, and if the amount of the base added is too small, gelation does not occur or gelation takes a long time, so a good quality film is formed. I can't get it. The base is added in an amount of 10 -5 to 1 mol, preferably 1 to 1 mol of the acid added in the previous step, per mol of the starting alkoxysilane.
It is appropriate to have a molar excess of 0 -4 to 10 -1 . If the excess amount of the base is more than 1 mol, a sharp increase in viscosity occurs, making it difficult to apply a film-like coating or gelling instantly.

【0016】加える水の量は原料のアルコキシシランの
種類にもよるが、前の工程と本工程で加えた水の添加量
の合計は、アルコキシシラン1モルに対し1〜100モ
ル、好ましくは2〜10モルである。1モルより少ない
と加水分解、ゲル化が十分に起こらず、多孔質膜を得る
ことができない。また100モルより多いと多孔質膜の
均質性が低下する。すでに前工程で十分量の水を加えて
いる場合には本工程で新たに水を加えなくてもよい。
The amount of water to be added depends on the type of the raw material alkoxysilane, but the total amount of water added in the previous step and this step is 1 to 100 mol, preferably 2 to 1 mol per mol of alkoxysilane. 10 to 10 mol. If the amount is less than 1 mol, hydrolysis and gelation do not sufficiently occur, and a porous membrane cannot be obtained. If the amount is more than 100 mol, the uniformity of the porous film is reduced. If a sufficient amount of water has already been added in the previous step, it is not necessary to newly add water in this step.

【0017】膜状塗布は流延、浸漬、スプレー法、回転
塗布法等の公知の方法で行う。膜厚は特に限定されない
が、0.1μm以上であることが好ましい。0.1μm
未満では多孔質膜の効果が十分に得られない。更に膜厚
1mm以下であることが短時間でゲルの乾燥を行うこと
ができることから好ましい。ゲルの乾燥に十分に時間を
かけることで1mmを超える膜厚の膜も作成することも
可能である。
The film-form coating is performed by a known method such as casting, dipping, spraying, and spin coating. The thickness is not particularly limited, but is preferably 0.1 μm or more. 0.1 μm
If it is less than 3, the effect of the porous membrane cannot be sufficiently obtained. Further, the thickness is preferably 1 mm or less because the gel can be dried in a short time. It is also possible to prepare a film having a thickness of more than 1 mm by taking sufficient time for drying the gel.

【0018】密着性、均質性、耐クラック性、耐剥離性
に優れた膜を得るために、基板上をあらかじめ密着向上
剤で処理してもよい。この場合の密着向上剤としてはい
わゆるシランカップリング剤として用いられるものを使
用することができる。好適に用いられるものとして3−
アミノプロピルトリメトキシシラン、3−アミノプロピ
ルトリエトキシシラン、N−(2−アミノエチル)−3
−アミノプロピルトリメトキシシラン、N−(2−アミ
ノエチル)−3−アミノプロピルメチルジメトキシシラ
ン、N−フェニル−3−アミノプロピルトリメトキシシ
ラン、3−メルカプトプロピルトリメトキシシラン、3
−クロロプロピルトリメトキシシラン、3−クロロプロ
ピルメチルジメトキシシラン、3−クロロプロピルメチ
ルジエトキシシラン、3−クロロプロピルメチルジクロ
ロシラン、ビニルトリクロロシラン、ビニルトリエトキ
シシラン、ビニルトリメトキシシラン、ビニルトリス
(2−メトキシエトキシ)シランなどが挙げられ、中で
も3−アミノプロピルトリメトキシシラン、3−アミノ
プロピルトリエトキシシラン、N−(2−アミノエチ
ル)−3−アミノプロピルトリメトキシシラン、N−
(2−アミノエチル)−3−アミノプロピルメチルジメ
トキシシランが特に好適に用いられる。これらの密着向
上剤を塗布するにあたっては必要に応じて他の添加物を
加えたり、アルコールや水などの溶媒で希釈して用いて
もよい。密着向上剤の塗布は流延、浸漬、スプレー法、
回転塗布法等の公知の方法で行う。塗布した後、過剰の
密着向上剤をアルコールなど一般の有機溶媒で洗浄除去
する。塗布から洗浄までの時間は通常数分間で十分であ
る。その後、洗浄溶媒を乾燥して処理基板をえる。塗布
から洗浄までの時間が短いと密着向上剤の効果が得られ
ず、逆に余り長いと密着向上剤が基板上で硬化すること
がある。
In order to obtain a film excellent in adhesion, homogeneity, crack resistance and peeling resistance, the substrate may be treated in advance with an adhesion improver. As the adhesion improver in this case, those used as a so-called silane coupling agent can be used. 3- is preferably used.
Aminopropyltrimethoxysilane, 3-aminopropyltriethoxysilane, N- (2-aminoethyl) -3
-Aminopropyltrimethoxysilane, N- (2-aminoethyl) -3-aminopropylmethyldimethoxysilane, N-phenyl-3-aminopropyltrimethoxysilane, 3-mercaptopropyltrimethoxysilane, 3
-Chloropropyltrimethoxysilane, 3-chloropropylmethyldimethoxysilane, 3-chloropropylmethyldiethoxysilane, 3-chloropropylmethyldichlorosilane, vinyltrichlorosilane, vinyltriethoxysilane, vinyltrimethoxysilane, vinyltris (2- Methoxyethoxy) silane, among which 3-aminopropyltrimethoxysilane, 3-aminopropyltriethoxysilane, N- (2-aminoethyl) -3-aminopropyltrimethoxysilane, N-
(2-Aminoethyl) -3-aminopropylmethyldimethoxysilane is particularly preferably used. When applying these adhesion improvers, other additives may be added as necessary, or they may be diluted with a solvent such as alcohol or water before use. The adhesion improver is applied by casting, dipping, spraying,
This is performed by a known method such as a spin coating method. After the application, the excess adhesion improver is removed by washing with a general organic solvent such as alcohol. A few minutes from application to washing is usually sufficient. Thereafter, the cleaning solvent is dried to obtain a processing substrate. If the time from application to washing is short, the effect of the adhesion improver cannot be obtained, and if too long, the adhesion improver may be cured on the substrate.

【0019】塗布した膜のゲル化反応の温度は0〜10
0℃の範囲であり、特に20〜60℃とするのが好まし
い。0℃未満では反応速度が小さく、十分な架橋を起こ
させるのに長時間を要し、また100℃を超える温度で
はボイドが生成しやすく、得られる多孔質膜の均質性が
低下する。ゲル化に要する時間はゲル化の温度や触媒の
量などによって異なるが、通常数分間〜数日間の範囲で
ある。
The temperature of the gelation reaction of the applied film is from 0 to 10
The temperature is in the range of 0 ° C, particularly preferably 20 to 60 ° C. If the temperature is lower than 0 ° C., the reaction rate is low, and it takes a long time to cause sufficient crosslinking. If the temperature is higher than 100 ° C., voids are easily formed, and the homogeneity of the obtained porous membrane is reduced. The time required for gelation varies depending on the gelling temperature, the amount of catalyst, and the like, but is usually in the range of several minutes to several days.

【0020】ゲル化を十分に進行させた後、溶媒を除去
するために乾燥する。乾燥温度は当然溶媒の種類によっ
て異なるが、通常20〜200℃の範囲で行う。ボイド
の発生を制御し、均質な乾燥ゲル膜を得るために、乾燥
工程中に徐々に温度を上昇させる方法も好ましい。この
乾燥ゲル膜から有機ポリマーのみを除去することにより
目的の多孔質ケイ素酸化物膜を得ることができる。有機
ポリマーを除去する方法としては加熱焼成、溶媒抽出、
プラズマ処理などが挙げられる。もっとも簡便なのがア
ミド結合含有有機ポリマーの熱分解温度以上で1〜24
時間程度加熱する方法である。
After the gelling has sufficiently proceeded, drying is performed to remove the solvent. The drying temperature depends on the type of the solvent, but is usually in the range of 20 to 200 ° C. In order to control the generation of voids and obtain a uniform dried gel film, a method of gradually increasing the temperature during the drying step is also preferable. The target porous silicon oxide film can be obtained by removing only the organic polymer from the dried gel film. As a method for removing the organic polymer, heat baking, solvent extraction,
Plasma treatment and the like can be mentioned. The simplest method is 1 to 24 at or above the thermal decomposition temperature of the amide bond-containing organic polymer.
This is a method of heating for about an hour.

【0021】本発明の方法では、テトラアルコキシシラ
ンの加水分解、脱水縮合が速やかに終了するので、溶媒
の蒸発による膜質の劣化を防ぎ、均一な多孔質膜を速や
かに得ることができる。
In the method of the present invention, since the hydrolysis and dehydration condensation of the tetraalkoxysilane are quickly completed, deterioration of the film quality due to evaporation of the solvent can be prevented, and a uniform porous film can be promptly obtained.

【0022】[0022]

【発明の実施の形態】以下に本発明の実施例を示す。な
お、実施例で得られたケイ素酸化物膜の評価は以下のよ
うに行った。 1.表面積(N2 BET) (株)島津製作所製の窒素吸着式表面積測定装置を用い
て測定した。 2.走査電子顕微鏡(SEM) 試料を約5mm四方に切断し、導電テープを貼った試料
台に載せカーボンペーストで導通を確保し、さらに白金
−パラジウムを1nm程度蒸着し、(株)日立製作所製
走査電子顕微鏡で測定を行った。電子の加速電圧は1k
Vに設定した。
Embodiments of the present invention will be described below. In addition, evaluation of the silicon oxide film obtained in the example was performed as follows. 1. Surface area (N2 BET) The surface area was measured using a nitrogen adsorption type surface area measuring device manufactured by Shimadzu Corporation. 2. Scanning Electron Microscope (SEM) A sample is cut into a square of about 5 mm, placed on a sample table on which a conductive tape is stuck, conduction is secured with a carbon paste, and platinum-palladium is vapor-deposited by about 1 nm, and a scanning electron microscope manufactured by Hitachi, Ltd. Measurements were taken with a microscope. Electron acceleration voltage is 1k
V was set.

【0023】[0023]

【実施例1】テトラエトキシシラン0.6gと、ポリ
(N−ビニルピロリドン)0.5gをエタノール0.8
g、ジメチルホルムアミド1.2gに溶解し、この溶液
に0.1N塩酸0.05g加え、室温にて5時間撹拌し
た。この溶液に0.1Nアンモニア水溶液0.5mlを
加え撹拌し、膜厚が1mmになるように速やかにガラス
基板上に流延塗布した後、密閉容器中で室温にて1時間
放置したところ、塗布膜は流動性を失っていた。終夜静
置し、5時間かけて60℃から150℃にて乾燥し、窒
素中で600℃にて12時間加熱した。得られたケイ素
酸化物膜は760m2 /gの表面積を有することが、窒
素吸着法により分かった。
Example 1 0.6 g of tetraethoxysilane and 0.5 g of poly (N-vinylpyrrolidone) were added to 0.8 g of ethanol.
g and dimethylformamide (1.2 g), and the solution was added with 0.1N hydrochloric acid (0.05 g) and stirred at room temperature for 5 hours. To this solution was added 0.5 ml of a 0.1N ammonia aqueous solution, followed by stirring. The solution was immediately cast onto a glass substrate so as to have a thickness of 1 mm, and then left standing at room temperature for 1 hour in a closed container. The membrane had lost fluidity. The mixture was allowed to stand overnight, dried at 60 ° C. to 150 ° C. for 5 hours, and heated at 600 ° C. for 12 hours in nitrogen. It was found by a nitrogen adsorption method that the obtained silicon oxide film had a surface area of 760 m 2 / g.

【0024】[0024]

【実施例2】シリコン基板上に3−アミノプロピルトリ
エトキシシランを流延塗布し、3分間放置した後メタノ
ールで洗浄し、60℃にて10分間乾燥した。10ml
容器に、テトラエトキシシラン1.2g、ポリ(N−ビ
ニルピロリドン)1.0gをエタノール1.6g、ジメ
チルホルムアミド2.4gに溶解し、この溶液に0.1
N塩酸0.1gを加え、室温にて3時間撹拌した。この
溶液に0.1Nアンモニア水溶液0.5mlを加え撹拌
し、膜厚が1μmになるように上記のシリコン基板上に
毎秒1500回転の速度で10秒間回転塗布した後、密
閉容器中で室温にて1時間放置した。終夜静置し、4時
間かけて60℃から160℃にて乾燥し、窒素中で60
0℃にて8時間加熱した。得られたケイ素酸化物膜の表
面を走査電子顕微鏡で観察したところ、非常に均一でク
ラックや巨大粒子の発生も見られなかった。
Example 2 3-Aminopropyltriethoxysilane was cast-coated on a silicon substrate, left for 3 minutes, washed with methanol, and dried at 60 ° C. for 10 minutes. 10ml
In a container, 1.2 g of tetraethoxysilane and 1.0 g of poly (N-vinylpyrrolidone) are dissolved in 1.6 g of ethanol and 2.4 g of dimethylformamide.
0.1 g of N hydrochloric acid was added, and the mixture was stirred at room temperature for 3 hours. 0.5 ml of a 0.1N ammonia aqueous solution was added to this solution, and the mixture was stirred and spin-coated on the silicon substrate at a speed of 1500 revolutions per second for 10 seconds so as to have a film thickness of 1 μm. Left for 1 hour. Allow to stand overnight, dry at 60 ° C. to 160 ° C. for 4 hours,
Heated at 0 ° C. for 8 hours. When the surface of the obtained silicon oxide film was observed with a scanning electron microscope, it was very uniform, and neither cracks nor giant particles were generated.

【0025】[0025]

【比較例1】テトラエトキシシラン5.2g、ポリ(N
−ビニルピロリドン)1.5gをエタノール2.5g、
ジメチルホルムアミド3.5gに溶解し、この溶液に
0.08N塩酸3.5g加え、室温にて3時間撹拌し
た。この溶液をガラス基板上に膜厚が1mmになるよう
に流延塗布した後、密閉容器中で室温にて終夜放置した
が、塗布膜は粘凋であり流動性を失っていなかった。
Comparative Example 1 5.2 g of tetraethoxysilane and poly (N
-Vinylpyrrolidone) 1.5 g ethanol 2.5 g,
It was dissolved in 3.5 g of dimethylformamide, and 3.5 g of 0.08 N hydrochloric acid was added to this solution, followed by stirring at room temperature for 3 hours. This solution was applied on a glass substrate by casting so as to have a thickness of 1 mm, and then left at room temperature overnight in a closed container. However, the applied film was viscous and did not lose its fluidity.

【0026】[0026]

【発明の効果】本発明で得られた多孔質ケイ素酸化物薄
膜は、従来法に比べて製造法がきわめて簡便かつ速やか
であるにもかかわらず良質のものである。また細孔径が
小さく、また空隙率を大きくできるため誘電率を低下さ
せることが可能なので、LSI多層配線用絶縁膜などに
用いることができる。その他、触媒の坦体としても使用
可能であることから、産業上大いに有用である。
The porous silicon oxide thin film obtained according to the present invention is of good quality in spite of its extremely simple and rapid production method as compared with the conventional method. In addition, since the dielectric constant can be reduced because the pore diameter is small and the porosity can be increased, it can be used as an insulating film for LSI multilayer wiring. In addition, since it can be used as a carrier for a catalyst, it is very useful in industry.

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】 アルコキシシランと、アミド結合を含有
する有機ポリマーを溶媒に溶解し、酸を添加して部分的
に加水分解した後、塩基触媒を添加して基板上に膜状に
塗布し加水分解、脱水縮合を行い、その後に溶媒を蒸発
させて得られた乾燥ゲルから有機ポリマーを除去するこ
とを特徴とする多孔質ケイ素酸化物膜の製造法。
1. An alkoxysilane and an organic polymer containing an amide bond are dissolved in a solvent and partially hydrolyzed by adding an acid. A method for producing a porous silicon oxide film, comprising performing decomposition, dehydration condensation, and then evaporating a solvent to remove an organic polymer from a dried gel obtained.
JP31366896A 1996-11-25 1996-11-25 Method for producing porous silicon oxide film Expired - Fee Related JP3851393B2 (en)

Priority Applications (1)

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JP31366896A JP3851393B2 (en) 1996-11-25 1996-11-25 Method for producing porous silicon oxide film

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JPH10158012A true JPH10158012A (en) 1998-06-16
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Cited By (8)

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Publication number Priority date Publication date Assignee Title
WO2001019922A1 (en) * 1999-09-16 2001-03-22 Hitachi Chemical Co., Ltd. Composition, methods of forming low-permittivity film from the composition, low-permittivity film, and electronic part having the low-permittivity film
US6479374B1 (en) * 1998-04-01 2002-11-12 Asahi Kasei Kabushiki Kaisha Method of manufacturing interconnection structural body
WO2003052003A1 (en) * 2001-12-14 2003-06-26 Asahi Kasei Kabushiki Kaisha Coating composition for forming low-refractive index thin layers
WO2017018543A1 (en) * 2015-07-30 2017-02-02 国立研究開発法人産業技術総合研究所 Silanol compound production method
KR20170099925A (en) * 2014-12-26 2017-09-01 닛토덴코 가부시키가이샤 Void structured film bonded through catalytic action and method for manufacturing same
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Cited By (13)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6479374B1 (en) * 1998-04-01 2002-11-12 Asahi Kasei Kabushiki Kaisha Method of manufacturing interconnection structural body
WO2001019922A1 (en) * 1999-09-16 2001-03-22 Hitachi Chemical Co., Ltd. Composition, methods of forming low-permittivity film from the composition, low-permittivity film, and electronic part having the low-permittivity film
KR100732089B1 (en) 1999-09-16 2007-06-27 히다치 가세고교 가부시끼가이샤 Composition, Methods of Forming Low-Permittivity Film from the Composition, Low-Permittivity Film, and Electronic Part Having the Low-Permittivity Film
WO2003052003A1 (en) * 2001-12-14 2003-06-26 Asahi Kasei Kabushiki Kaisha Coating composition for forming low-refractive index thin layers
US7081272B2 (en) 2001-12-14 2006-07-25 Asahi Kasei Kabushiki Kaisha Coating composition for forming low-refractive index thin layers
KR20170099925A (en) * 2014-12-26 2017-09-01 닛토덴코 가부시키가이샤 Void structured film bonded through catalytic action and method for manufacturing same
KR20170101230A (en) * 2014-12-26 2017-09-05 닛토덴코 가부시키가이샤 Porous silicone object and process for producing same
US11618807B2 (en) 2014-12-26 2023-04-04 Nitto Denko Corporation Film with void spaces bonded through catalysis and method of producing the same
WO2017018543A1 (en) * 2015-07-30 2017-02-02 国立研究開発法人産業技術総合研究所 Silanol compound production method
JPWO2017018543A1 (en) * 2015-07-30 2018-05-24 国立研究開発法人産業技術総合研究所 Method for producing silanol compound
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