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JP4305612B2 - Metal oxide ultrafine particles and method for producing the same - Google Patents
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JP4305612B2 - Metal oxide ultrafine particles and method for producing the same - Google Patents

Metal oxide ultrafine particles and method for producing the same Download PDF

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Publication number
JP4305612B2
JP4305612B2 JP2002223709A JP2002223709A JP4305612B2 JP 4305612 B2 JP4305612 B2 JP 4305612B2 JP 2002223709 A JP2002223709 A JP 2002223709A JP 2002223709 A JP2002223709 A JP 2002223709A JP 4305612 B2 JP4305612 B2 JP 4305612B2
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metal
metal oxide
organic compound
temperature
ultrafine particles
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JP2004059407A (en
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昌美 中許
正喜 豊田
晋也 古田
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株式会社巴製作所
地方独立行政法人 大阪市立工業研究所
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Description

【0001】
【発明の属する技術分野】
本発明は、金属酸化物超微粒子及びその製造方法に関する。
【0002】
【従来技術】
100nm以下の金属酸化物超微粒子では、金属酸化物の性質は一般の粒子サイズのものとは大きく異なる性質を示すことが知られている。例えば、単位体積当たりの表面積が大きいことから、高い触媒活性等を示す。また、焼結温度もバルク材料に比べると低いため、導電性酸化物として知られている酸化スズ、酸化インジウム等では、大面積の透明導電膜を形成する材料として期待されている。
【0003】
このような金属酸化物微粒子の製造方法としては、従来は大きな固体粒子を砕いて微粒子とする粉砕法が工業的に広く利用されている。ところが、サブミクロンレベルの大きさが限界であり、金属酸化物超微粒子製造のためにはナノレベルでの粒子設計が可能な気相法又は液相法に頼らざるを得ない。
【0004】
気相法としては、原料の金属を加熱して蒸発させ、アルゴン、ヘリウム等の不活性雰囲気ガス中で凝集させて金属酸化物超微粒子を製造する蒸発凝縮法、蒸気圧の高い金属塩化物、揮発性オキシ塩化物、金属アルコキシド、有機金属化合物等を原料化合物として使用し、高温で加熱分解させる気相反応法等がある。しかし、蒸発凝縮法では、高価なアルゴン、ヘリウム等を使用しなければならず、コスト面で非常に不利である。気相反応法では、原料化合物が反応性が高い、取り扱いが困難であり、取扱い性、安全性等という点で問題がある。
【0005】
しかも、これらの製造法では、いずれも加熱法として抵抗加熱法、電気炉法、高周波誘導加熱法、プラズマ加熱法、電子ビーム加熱法、レーザービーム加熱法等が採用されているため、特殊な装置が必要である。
【0006】
一方、液相法としては、金属塩水溶液又は金属アルコキシドから化学反応により固体粒子を析出させる化学沈殿法、金属アルコキシドの加水分解と重縮合反応からシリカコロイドや酸化チタン金属酸化物超微粒子を得るアルコキシド法、高温高圧の水熱条件を利用する水熱合成法等がある。しかし、いずれの方法でも、生成した粒子の凝集が問題となる。
【0007】
他方、金属塩溶液を高温雰囲気に噴霧し、溶媒の蒸発と金属塩の熱分解を一段で行って粉体を合成する噴霧熱分解法で酸化ジルコニウム、酸化チタン等の微粒子を合成する方法もある。しかし、この方法では中空状の粒子又はその破砕粒子の形で得られることが多い。このため、中実状の金属酸化物超微粒子を得るためには、より高温での焼結・溶融が必要とされる。
【0008】
このように、従来技術では、金属酸化物超微粒子を効率的に製造することが困難であり、しかも得られる金属酸化物超微粒子は依然として凝集等の点で物性面に問題がある。
【0009】
【発明が解決しようとする課題】
上記のような現状に鑑み、分散安定性に優れた金属酸化物超微粒子を工業的規模で生産する上において、新たな技術の開発が必要とされている。
【0010】
従って、本発明は、分散安定性に優れた金属酸化物超微粒子を工業的規模で製造することを主な目的とする。
【0011】
【課題を解決するための手段】
本発明者は、上記の従来技術の問題に鑑み、鋭意研究を重ねた結果、特定の製造方法により得られる金属酸化物超微粒子は、その特異な構成に基づき特有の性質を発現することを見出し、本発明を完成するに至った。
【0012】
すなわち、本発明は、下記の金属酸化物超微粒子及びその製造方法に係るものである。
【0016】
1. 金属酸化物超微粒子からなる粉末の製造方法であって、粉末状又は液状の金属有機化合物を、酸化性雰囲気下において、その金属有機化合物の有機質成分の分解開始温度以上、かつ、400℃未満の温度で加熱し、金属酸化物及び有機成分を含有し、前記金属酸化物を50〜95重量%含有する微粒子を得ることを特徴とする方法
2. 加熱温度が200℃以上400℃未満である、前記項1記載の製造方法。
3. 金属有機化合物が、脂肪酸の金属塩である前記項1又は2に記載の製造方法。
4. 脂肪酸の炭素数が5〜30である前記項3記載の製造方法。
【0020】
【発明の実施の形態】
(1)本発明金属酸化物超微粒子
本発明の金属酸化物超微粒子は、金属酸化物及び有機成分を含有する微粒子であって、その平均粒径が1〜100nmであることを特徴とする。
【0021】
本発明において、有機成分は、本発明の分散安定性を維持できるものであれば特に限定されない。特に、金属有機化合物に由来する有機成分が好ましい。すなわち、後記の本発明製造方法に示すように、金属有機化合物を所定の条件下で加熱された場合に残存する有機成分が好適である。
【0022】
上記のような金属有機化合物としては、有機金属化合物のほか、金属アルコキシド等も包含する。金属有機化合物としては、特に制限されず、またいずれの市販品も使用できる。例えば、ナフテン酸塩、オクチル酸塩、ステアリン酸塩、一般式C65(CH2nCOOH (nは0〜5の整数が好ましい。)で示されるカルボン酸類(例えば、安息香酸等)の塩、パラトルイル酸塩、n−デカン酸塩等の脂肪酸金属塩、イソプロポキシド、エトキシド等の金属アルコキシド、上記金属のアセチルアセトン錯塩等が挙げられる。これらの中でも、特にオレイン酸塩、パラトルイル酸塩、ステアリン酸塩、n−デカン酸塩、金属エトキシド、金属アセチルアセトネート等が好ましい。
【0023】
これらの中でも、脂肪酸塩(脂肪酸の金属塩)が好ましい。特に、飽和脂肪酸の金属塩が望ましい。飽和脂肪酸としては、例えば下記一般的で示されるような脂肪酸が好適である。
【0024】
n2n+1COOH(ただし、nは5〜30の整数を示す。)
上記n(脂肪酸の炭素数)は限定的ではないが、通常5〜30程度、特に5〜20、さらに6〜18であることが好ましい。
【0025】
金属有機化合物に含有される金属は特に限定されず、金属酸化物超微粒子の用途等に応じて適宜選択することができる。好ましくはCu、Zn、In、Si、Ge、Sn、Fe、Co、Ni、Ru、Rh、Os、Ir、V、Cr、Mn、Y、Ti、Zr、Nb、Mo、Ca、Ba、Sb及びBiの少なくとも1種を含む金属有機化合物を好ましく使用することができる。
【0026】
また、金属有機化合物は、単独で又は2種以上併用することができる。金属有機化合物の金属も特に制限されず、最終製品の用途等に応じて適宜選択することができる。
【0027】
上記の金属成分は、上記金属有機化合物に由来するものであれば特に制限されない。すなわち、用いる金属有機化合物に存在していた金属成分であれば良い。金属成分としては、好ましくはCu、Zn、In、Si、Ge、Sn、Fe、Co、Ni、Ru、Rh、Os、Ir、V、Cr、Mn、Y、Ti、Zr、Nb、Mo、Ca、Ba、Sb及びBiの少なくとも1種である。本発明の金属成分としては、これらの金属単身、これらの金属の混合物、あるいはこれらの金属の合金等のあらゆる状態を包含する。
【0028】
本発明の金属酸化物超微粒子における金属酸化物成分の比率は、最終製品の用途等に応じて適宜設定できるが、通常は50〜95重量%程度、好ましくは60〜95重量%とすれば良い。残部は、有機成分以外の成分が含まれていても良いが、実質的に有機成分からなることが望ましい。
【0029】
金属酸化物超微粒子の平均粒径は、通常1〜100nm程度であるが、最終製品の用途等により変更することが可能である。例えば、金属コーティング用に用いる場合は通常1〜50nm程度、好ましくは1〜10nmとすれば良い。
(2)金属酸化物超微粒子の製造方法
本発明の金属酸化物超微粒子は、例えば金属有機化合物を、酸化性雰囲気下において、その金属有機化合物の分解開始温度以上、かつ、完全分解温度未満の温度範囲内で加熱することによって製造することができる。
【0030】
金属有機化合物としては、特にその種類は制限されず、前記(1)で挙げたものを使用することができる。これらの中でも、特にオレイン酸塩、パラトルイル酸塩、ステアリン酸塩、一般式C65(CH2nCOOH (n=0〜5の整数が好ましい。)で示されるカルボン酸類(例えば、安息香酸等)の塩、n−デカン酸塩、金属エトキシド、金属アセチルアセトネート等が好ましい。より好ましくは、前記(1)で挙げた脂肪酸塩である。すなわち、上記脂肪酸としては、下記一般的で示されるような脂肪酸が好適である。
【0031】
n2n+1COOH(ただし、nは5〜30の整数)
上記n(脂肪酸の炭素数)は限定的ではないが、通常5〜30程度、特に5〜20、さらに6〜18であることが好ましい。
【0032】
金属有機化合物の金属成分については、例えばそれより得られる金属酸化物超微粒子を金属コーティング膜用に用いる場合は、その金属成分が主として金属コーティング膜を形成することになるので、その用途等に応じて適宜選択すれば良い。
【0033】
なお、例えば昇華性があったり、急激に分解する等の特性を有する金属有機化合物であっても、昇華性を押さえるために高沸点の溶剤を加える等の工夫により有効に使用することができる。
【0034】
また、本発明方法では、例えば2種以上の金属を含む金属有機化合物を予め混合することによって複合型の金属酸化物超微粒子を調製することも可能である。
【0035】
原料としての金属有機化合物の形態は特に制限されず、粉末状、液状等のいずれのものであっても良い。
【0036】
加熱温度は、金属有機化合物が完全に分解しない限り特に制限されない。すなわち、その金属有機化合物の分解開始温度以上、かつ、完全分解温度未満の温度範囲内とすれば良い。分解開始温度とは、その金属有機化合物の有機質成分が分解しはじめる温度をいい、また完全分解温度とはその金属有機化合物の有機質成分が完全に分解してしまう温度をいう。本発明では、この温度範囲内において、金属有機化合物の種類等に応じて適宜設定することができる。例えば、分解開始温度が約200℃であり、完全分解温度が約400℃である金属有機化合物の場合、200℃〜400℃の温度範囲内に加熱温度を保持すれば良い。なお、保持時間は、加熱温度等に応じて適宜変更することができる。
【0037】
加熱温度の上限は、特に、用いる金属有機化合物が熱分解してその重量が当初の50%に減少する温度を上限として設定することが望ましい。
【0038】
加熱雰囲気は、酸化性雰囲気であれば良く、例えば大気中、酸素ガス雰囲気中等のいずれであっても良い。また、窒素、二酸化炭素、アルゴン、ヘリウム等の不活性ガスで希釈しても良い。
【0039】
また、加熱するに際し、金属有機化合物に各種アルコール類を添加することもできる。これにより、加熱温度を低くできる等の効果が得られる。アルコール類としては、少なくとも上記効果が得られる限り特に制限されず、例えばグリセリン、エチレングリコール、ラウリルアルコール等が挙げられる。アルコール類の添加量は、用いるアルコールの種類等に応じて適宜定めることができるが、通常は金属有機化合物100重量部に対して5〜20重量部程度、好ましくは10〜15重量部とすれば良い。
【0040】
さらに、本発明の製造方法では、これらの成分以外にも、本発明の効果を妨げない範囲において、流動パラフィン、各種石油系高沸点溶媒、油脂等の公知の各種添加剤を配合することによって作業性等を改善することが可能である。
【0041】
加熱が終了した後、必要に応じて精製を行う。精製方法は、公知の精製法も適用でき、例えば遠心分離、膜精製、溶媒抽出等により行えば良い。
【0042】
【発明の効果】
本発明の製造方法では、特に金属有機化合物を一定雰囲気下で比較的低温で加熱処理することにより、従来の超微粒子とは異なる金属酸化物超微粒子を効率的に得ることができる。
【0043】
すなわち、本発明の金属酸化物超微粒子は、金属酸化物とともに有機成分を含むため、分散安定性に優れ、溶剤に分散させると可溶化状態となる。例えば、そのままトルエン、ヘキサン、ケロシン等に分散して用いても良く、また公知のペースト化剤に配合してペーストとして用いることもできる。
【0044】
このような特徴をもつ本発明の金属酸化物超微粒子は、金属酸化物の種類に応じて優れた特性(触媒活性、導電性、透光性、紫外線遮蔽性、熱線遮蔽性、抗菌性、防汚性、防錆性、防食性等)を得ることができる。このため、電子材料(プリント配線、導電性材料、透明膜、光学素子等)、磁性材料(磁気記録媒体、電磁波吸収体、電磁波共鳴器等)、触媒材料(高速反応触媒、センサー等)、構造材料(遠赤外材料、複合皮膜形成材等)、セラミックス・金属材料(焼結助剤、コーティング材料等)、医療材料等の各種の用途に幅広く用いることが可能である。
【0045】
【実施例】
以下、実施例を示し、本発明の特徴とするところをより一層明確にする。実施例における各物性の測定は、次のようにして実施した。
(1)定性分析
金属酸化物の同定は、強力X線回折装置「MXP18」(マックサイエンス社製)を用い、粉末X線回折分析法により測定した。
【0046】
有機基の同定は、NMR測定装置「JOEL JNM−EX270FT−NMR」(日本電子社製)を用いてH1−NMRスペクトル(溶媒:重クロロホルムCDCl3溶媒)を測定した。
(2)平均粒子径
透過型電子顕微鏡「JEM1200EX」(日本電子社製)により観察し、任意に選んだ100個の粒子の粒径の算術平均値を平均粒子径とした。
(3)金属成分の含有量
熱分析装置「SSC/5200」(セイコー電子工業)を用い、TG/DTA分析することにより求めた。
【0047】
実施例1
ミリスチン酸スズ(C1327COO)2Sn(10g)を四つ口フラスコに固体のまま入れ、空気を供給しながら300℃まで徐々に加熱した。300℃で8時間保持した後、放冷した。生成した粉末をエタノールで繰り返し洗浄した後、桐山ロートでろ別し、減圧下で乾燥させた。
【0048】
得られた粉末を粉末X線回折分析、NMR分析、TEM観察及び熱分析した。粉末X線回折分析の結果を図1に示す。TEMによる観察結果(イメージ図)を図2に示す。得られた粉末はXRDにより酸化スズ(SnO2)と同定され、TEMからその平均粒子径は10nmであった。金属酸化物成分の含有量は、TG/DTA分析から80.3%で、有機成分が共存することが分かった。有機成分については、NMRから0.5〜1.5ppmにかけてアルキル鎖のメチレン、メチル基に帰属されるシグナルが観測された。
【0049】
実施例2
デカン酸スズ(C919COO)2Sn(10g)を四つ口フラスコに固体のまま入れ、空気を供給しながら270℃まで徐々に加熱した。270℃で8時間保持した後、放冷した。生成した粉末をエタノールで繰り返し洗浄した後、桐山ロートでろ別し、減圧下で乾燥させた。
【0050】
得られた粉末は酸化スズ(SnO2)と同定され、その平均粒子径は8nm であった。金属酸化物成分の含有量は72.1重量%で、アルキル鎖のメチレン、メチル基のシグナルが0.5〜1.5ppmに観測された。
【0051】
実施例3
ミリスチン酸インジウム(C1327COO)3In(10g)を四つ口フラスコに固体のまま入れ、空気を供給しながら320℃まで徐々に加熱した。320℃で5時間保持した後、放冷した。生成した粉末をエタノールで繰り返し洗浄した後、桐山ロートでろ別し、減圧下で乾燥させた。
【0052】
得られた粉末を粉末X線回折分析、NMR分析、TEM観察及び熱分析した。粉末X線回折分析の結果を図3に示す。TEMによる観察結果(イメージ図)を図4に示す。得られた粉末は酸化インジウム(In23)と同定された。その平均粒子径は20nmであった。金属酸化物成分の含有量は熱分析により91.6重量%で、有機成分としてはNMRより0.8〜1.6ppmにかけてアルキル鎖のメチレン、メチル基のシグナルが観測された。
【0053】
実施例4
デカン酸インジウム(C919COO)3In(10g)を四つ口フラスコに固体のまま入れ、空気を供給しながら100℃まで加熱することにより完全に融解させた後、340℃まで徐々に加熱した。340℃で8時間保持した後、放冷した。生成した粉末をエタノールで繰り返し洗浄した後、桐山ロートでろ別し、減圧下で乾燥させた。
【0054】
得られた粉末は酸化インジウム(In23)と同定された。また、その平均粒子径は26nmであった。金属酸化物成分の含有量は、96.6重量%であった有機成分としてNMRより0.8〜1.6ppmにかけてアルキル鎖のメチレン、メチル基のシグナルが観測された。
【0055】
実施例5
デカン酸亜鉛(C919COO)2Zn(10g)を四つ口フラスコに固体のまま入れ、空気を供給しながら320℃まで徐々に加熱した。320℃で8時間保持した後、放冷した。生成した粉末をメタノールで繰り返し洗浄した後、桐山ロートでろ別し、減圧下で乾燥させた。
【0056】
得られた粉末は粉末X線回折分析から酸化亜鉛(ZnO)と同定された。その平均粒子径は85nm であった。金属酸化物成分の含有量は、95.1重量%であった。アルキル鎖のメチレン、メチル基のシグナルがNMRにおいて0.5〜1.5ppmにかけて観測されることから、有機成分として共存していることが分かった。
【図面の簡単な説明】
【図1】実施例1で得られた粉末の粉末X線回折分析の結果を示す。
【図2】実施例1で得られた粉末のTEMによる観察結果を示すイメージ図である。
【図3】実施例3で得られた粉末の粉末X線回折分析を行った結果を示す。
【図4】実施例3で得られた粉末のTEMによる観察結果を示すイメージ図である。
[0001]
BACKGROUND OF THE INVENTION
The present invention relates to metal oxide ultrafine particles and a method for producing the same.
[0002]
[Prior art]
In metal oxide ultrafine particles of 100 nm or less, it is known that the properties of metal oxides are significantly different from those of general particle sizes. For example, since the surface area per unit volume is large, high catalytic activity and the like are exhibited. In addition, since the sintering temperature is lower than that of the bulk material, tin oxide, indium oxide, and the like known as conductive oxides are expected as materials for forming a large-area transparent conductive film.
[0003]
As a method for producing such metal oxide fine particles, a pulverization method in which large solid particles are crushed into fine particles has been widely used industrially. However, the size at the sub-micron level is the limit, and for producing metal oxide ultrafine particles, it is necessary to rely on a gas phase method or a liquid phase method capable of designing particles at the nano level.
[0004]
As the vapor phase method, the raw material metal is heated to evaporate and agglomerated in an inert atmosphere gas such as argon or helium to produce ultrafine particles of metal oxide, metal chloride with high vapor pressure, There are gas phase reaction methods in which volatile oxychlorides, metal alkoxides, organometallic compounds and the like are used as raw material compounds and thermally decomposed at high temperatures. However, in the evaporation condensation method, expensive argon, helium, etc. must be used, which is very disadvantageous in terms of cost. In the gas phase reaction method, the raw material compound has high reactivity, is difficult to handle, and has problems in terms of handleability and safety.
[0005]
In addition, these manufacturing methods employ a resistance heating method, an electric furnace method, a high-frequency induction heating method, a plasma heating method, an electron beam heating method, a laser beam heating method, etc. as a heating method. is required.
[0006]
On the other hand, the liquid phase method includes a chemical precipitation method in which solid particles are precipitated from a metal salt aqueous solution or metal alkoxide by a chemical reaction, and an alkoxide that obtains silica colloid or titanium oxide metal oxide ultrafine particles from hydrolysis and polycondensation reaction of metal alkoxide. And hydrothermal synthesis using high-temperature and high-pressure hydrothermal conditions. However, in any method, the aggregation of the generated particles becomes a problem.
[0007]
On the other hand, there is also a method of synthesizing fine particles such as zirconium oxide and titanium oxide by spray pyrolysis method in which a metal salt solution is sprayed in a high temperature atmosphere and solvent evaporation and metal salt pyrolysis are performed in one step to synthesize powder. . However, this method is often obtained in the form of hollow particles or crushed particles thereof. For this reason, in order to obtain solid metal oxide ultrafine particles, sintering and melting at higher temperatures are required.
[0008]
Thus, in the prior art, it is difficult to efficiently produce metal oxide ultrafine particles, and the obtained metal oxide ultrafine particles still have problems in physical properties in terms of aggregation and the like.
[0009]
[Problems to be solved by the invention]
In view of the current situation as described above, development of a new technology is required for producing ultrafine metal oxide particles having excellent dispersion stability on an industrial scale.
[0010]
Accordingly, the main object of the present invention is to produce ultrafine metal oxide particles having excellent dispersion stability on an industrial scale.
[0011]
[Means for Solving the Problems]
As a result of intensive studies in view of the above-described problems of the prior art, the present inventor has found that the metal oxide ultrafine particles obtained by a specific production method develop a unique property based on its unique configuration. The present invention has been completed.
[0012]
That is, the present invention relates to the following metal oxide ultrafine particles and a method for producing the same.
[0016]
1. A method for producing a powder comprising ultrafine metal oxide particles, wherein a powdered or liquid metal organic compound is heated in an oxidizing atmosphere to a temperature not less than the decomposition start temperature of the organic component of the metal organic compound and less than 400 ° C. method was heated at a temperature, containing a metal oxide and an organic component, characterized in that said metal oxide to obtain a fine particle containing 50 to 95 wt%.
2. The manufacturing method of said claim | item 1 whose heating temperature is 200 degreeC or more and less than 400 degreeC.
3. Item 3. The method according to Item 1 or 2, wherein the metal organic compound is a metal salt of a fatty acid.
4). Item 4. The method according to Item 3, wherein the fatty acid has 5 to 30 carbon atoms.
[0020]
DETAILED DESCRIPTION OF THE INVENTION
(1) Metal oxide ultrafine particles of the present invention The metal oxide ultrafine particles of the present invention are fine particles containing a metal oxide and an organic component and have an average particle diameter of 1 to 100 nm.
[0021]
In the present invention, the organic component is not particularly limited as long as the dispersion stability of the present invention can be maintained. In particular, an organic component derived from a metal organic compound is preferable. That is, as shown in the production method of the present invention described later, an organic component remaining when the metal organic compound is heated under predetermined conditions is preferable.
[0022]
Examples of the metal organic compound as described above include metal alkoxide and the like in addition to the organic metal compound. The metal organic compound is not particularly limited, and any commercially available product can be used. For example, carboxylic acids represented by naphthenate, octylate, stearate, general formula C 6 H 5 (CH 2 ) n COOH (n is preferably an integer of 0 to 5) (for example, benzoic acid, etc.) Salts, fatty acid metal salts such as p-toluoylate and n-decanoate, metal alkoxides such as isopropoxide and ethoxide, and acetylacetone complex salts of the above metals. Among these, oleate, p-toluate, stearate, n-decanoate, metal ethoxide, metal acetylacetonate and the like are particularly preferable.
[0023]
Of these, fatty acid salts (metal salts of fatty acids) are preferred. In particular, metal salts of saturated fatty acids are desirable. As the saturated fatty acid, for example, the following general fatty acids are suitable.
[0024]
C n H 2n + 1 COOH (where n represents an integer of 5 to 30)
The n (the number of carbon atoms of the fatty acid) is not limited, but is usually about 5 to 30, particularly 5 to 20, and further preferably 6 to 18.
[0025]
The metal contained in the metal organic compound is not particularly limited, and can be appropriately selected according to the use of the metal oxide ultrafine particles. Preferably Cu, Zn, In, Si, Ge, Sn, Fe, Co, Ni, Ru, Rh, Os, Ir, V, Cr, Mn, Y, Ti, Zr, Nb, Mo, Ca, Ba, Sb and A metal organic compound containing at least one of Bi can be preferably used.
[0026]
Moreover, a metal organic compound can be used individually or in combination of 2 or more types. The metal of the metal organic compound is not particularly limited, and can be appropriately selected according to the use of the final product.
[0027]
The metal component is not particularly limited as long as it is derived from the metal organic compound. That is, any metal component that exists in the metal organic compound used may be used. The metal component is preferably Cu, Zn, In, Si, Ge, Sn, Fe, Co, Ni, Ru, Rh, Os, Ir, V, Cr, Mn, Y, Ti, Zr, Nb, Mo, Ca. , Ba, Sb and Bi. The metal component of the present invention includes all states such as a single metal, a mixture of these metals, or an alloy of these metals.
[0028]
The ratio of the metal oxide component in the ultrafine metal oxide particles of the present invention can be appropriately set according to the use of the final product, but is usually about 50 to 95% by weight, preferably 60 to 95% by weight. . The balance may contain components other than organic components, but it is desirable that the balance is substantially composed of organic components.
[0029]
The average particle diameter of the metal oxide ultrafine particles is usually about 1 to 100 nm, but can be changed depending on the use of the final product. For example, when used for metal coating, it is usually about 1 to 50 nm, preferably 1 to 10 nm.
(2) Method for Producing Metal Oxide Ultrafine Particles The metal oxide ultrafine particles of the present invention have, for example, a metal organic compound that is not less than the decomposition start temperature of the metal organic compound and less than the complete decomposition temperature in an oxidizing atmosphere. It can manufacture by heating within a temperature range.
[0030]
The type of the metal organic compound is not particularly limited, and those mentioned in the above (1) can be used. Among these, carboxylic acids (for example, benzoate) represented by oleate, p-toluate, stearate, and general formula C 6 H 5 (CH 2 ) n COOH (n is preferably an integer of 0 to 5). Acid) salt, n-decanoate, metal ethoxide, metal acetylacetonate and the like are preferable. More preferred are the fatty acid salts mentioned in (1) above. That is, as the above fatty acid, the following general fatty acids are suitable.
[0031]
C n H 2n + 1 COOH (where n is an integer of 5 to 30)
The n (the number of carbon atoms of the fatty acid) is not limited, but is usually about 5 to 30, particularly 5 to 20, and further preferably 6 to 18.
[0032]
Regarding the metal component of the metal organic compound, for example, when the metal oxide ultrafine particles obtained from the metal organic compound are used for a metal coating film, the metal component mainly forms a metal coating film. May be selected as appropriate.
[0033]
For example, even a metal organic compound having properties such as sublimability and rapid decomposition can be effectively used by adding a high-boiling solvent to suppress sublimation.
[0034]
In the method of the present invention, it is also possible to prepare composite type metal oxide ultrafine particles by previously mixing, for example, a metal organic compound containing two or more metals.
[0035]
The form of the metal organic compound as a raw material is not particularly limited, and any form such as powder or liquid may be used.
[0036]
The heating temperature is not particularly limited as long as the metal organic compound is not completely decomposed. In other words, the temperature may be within the temperature range above the decomposition start temperature of the metal organic compound and below the complete decomposition temperature. The decomposition start temperature is a temperature at which the organic component of the metal organic compound begins to decompose, and the complete decomposition temperature is a temperature at which the organic component of the metal organic compound is completely decomposed. In this invention, it can set suitably according to the kind etc. of a metal organic compound within this temperature range. For example, in the case of a metal organic compound having a decomposition start temperature of about 200 ° C. and a complete decomposition temperature of about 400 ° C., the heating temperature may be maintained within a temperature range of 200 ° C. to 400 ° C. The holding time can be changed as appropriate according to the heating temperature and the like.
[0037]
The upper limit of the heating temperature is particularly preferably set at the temperature at which the metal organic compound to be used is thermally decomposed and its weight is reduced to 50% of the original.
[0038]
The heating atmosphere may be an oxidizing atmosphere, and may be, for example, in the air or in an oxygen gas atmosphere. Moreover, you may dilute with inert gas, such as nitrogen, a carbon dioxide, argon, and helium.
[0039]
Moreover, when heating, various alcohols can also be added to a metal organic compound. Thereby, the effect that the heating temperature can be lowered is obtained. Alcohols are not particularly limited as long as at least the above effects are obtained, and examples thereof include glycerin, ethylene glycol, and lauryl alcohol. The amount of alcohol added can be appropriately determined according to the type of alcohol used, etc., but is usually about 5 to 20 parts by weight, preferably 10 to 15 parts by weight with respect to 100 parts by weight of the metal organic compound. good.
[0040]
Further, in the production method of the present invention, in addition to these components, work can be performed by blending various known additives such as liquid paraffin, various petroleum-based high-boiling solvents, fats and oils, etc. within a range not impeding the effects of the present invention. It is possible to improve the sex and the like.
[0041]
After the heating is completed, purification is performed as necessary. As a purification method, a known purification method can be applied. For example, centrifugation, membrane purification, solvent extraction and the like may be performed.
[0042]
【The invention's effect】
In the production method of the present invention, metal oxide ultrafine particles different from conventional ultrafine particles can be efficiently obtained, particularly by heat-treating a metal organic compound at a relatively low temperature under a constant atmosphere.
[0043]
That is, since the metal oxide ultrafine particles of the present invention contain an organic component together with the metal oxide, the metal oxide ultrafine particles are excellent in dispersion stability and become solubilized when dispersed in a solvent. For example, it may be used as it is by dispersing in toluene, hexane, kerosene, etc., or it may be blended with a known pasting agent and used as a paste.
[0044]
The metal oxide ultrafine particles of the present invention having such characteristics have excellent characteristics (catalytic activity, conductivity, translucency, ultraviolet shielding, heat ray shielding, antibacterial, antibacterial properties) depending on the type of metal oxide. Dirty, rustproof, anticorrosive, etc.) can be obtained. For this reason, electronic materials (printed wiring, conductive materials, transparent films, optical elements, etc.), magnetic materials (magnetic recording media, electromagnetic wave absorbers, electromagnetic wave resonators, etc.), catalyst materials (fast reaction catalysts, sensors, etc.), structures It can be widely used for various applications such as materials (far infrared materials, composite film forming materials, etc.), ceramics / metal materials (sintering aids, coating materials, etc.), medical materials and the like.
[0045]
【Example】
Hereinafter, examples will be shown to further clarify the features of the present invention. Each physical property in the examples was measured as follows.
(1) Qualitative analysis The metal oxide was identified by a powder X-ray diffraction analysis method using a powerful X-ray diffractometer "MXP18" (manufactured by Mac Science).
[0046]
The organic group was identified by measuring an H1-NMR spectrum (solvent: deuterated chloroform CDCl 3 solvent) using an NMR measuring apparatus “JOEL JNM-EX270FT-NMR” (manufactured by JEOL Ltd.).
(2) Average particle size The average particle size was determined by observing with a transmission electron microscope “JEM1200EX” (manufactured by JEOL Ltd.), and the arithmetic average value of the particle sizes of 100 particles arbitrarily selected.
(3) Content of metal component It was determined by TG / DTA analysis using a thermal analyzer “SSC / 5200” (Seiko Electronics Industry).
[0047]
Example 1
Tin myristate (C 13 H 27 COO) 2 Sn (10 g) was placed as a solid in a four-necked flask and gradually heated to 300 ° C. while supplying air. After holding at 300 ° C. for 8 hours, it was allowed to cool. The produced powder was repeatedly washed with ethanol, filtered with a Kiriyama funnel, and dried under reduced pressure.
[0048]
The obtained powder was subjected to powder X-ray diffraction analysis, NMR analysis, TEM observation and thermal analysis. The result of the powder X-ray diffraction analysis is shown in FIG. The observation result (image figure) by TEM is shown in FIG. The obtained powder was identified as tin oxide (SnO 2 ) by XRD, and the average particle diameter was 10 nm from TEM. The content of the metal oxide component was 80.3% from TG / DTA analysis, and it was found that the organic component coexists. For the organic component, signals attributable to methylene and methyl groups of the alkyl chain were observed from NMR to 0.5 to 1.5 ppm.
[0049]
Example 2
Tin decanoate (C 9 H 19 COO) 2 Sn (10 g) was placed as a solid in a four-necked flask and gradually heated to 270 ° C. while supplying air. After holding at 270 ° C. for 8 hours, the mixture was allowed to cool. The produced powder was repeatedly washed with ethanol, filtered with a Kiriyama funnel, and dried under reduced pressure.
[0050]
The obtained powder was identified as tin oxide (SnO 2 ), and the average particle size was 8 nm. The content of the metal oxide component was 72.1% by weight, and signals of methylene and methyl groups in the alkyl chain were observed at 0.5 to 1.5 ppm.
[0051]
Example 3
Indium myristate (C 13 H 27 COO) 3 In (10 g) was placed as a solid in a four-necked flask and gradually heated to 320 ° C. while supplying air. After holding at 320 ° C. for 5 hours, it was allowed to cool. The produced powder was repeatedly washed with ethanol, filtered with a Kiriyama funnel, and dried under reduced pressure.
[0052]
The obtained powder was subjected to powder X-ray diffraction analysis, NMR analysis, TEM observation and thermal analysis. The result of the powder X-ray diffraction analysis is shown in FIG. The observation result (image figure) by TEM is shown in FIG. The resulting powder was identified as indium oxide (In 2 O 3 ). The average particle size was 20 nm. The content of the metal oxide component was 91.6 wt% by thermal analysis, and signals of methylene and methyl groups in the alkyl chain were observed as the organic component from 0.8 to 1.6 ppm from NMR.
[0053]
Example 4
Indium decanoate (C 9 H 19 COO) 3 In (10 g) is placed in a four-necked flask as a solid, and is completely melted by heating to 100 ° C. while supplying air, and then gradually increased to 340 ° C. Heated. After holding at 340 ° C. for 8 hours, it was allowed to cool. The produced powder was repeatedly washed with ethanol, filtered with a Kiriyama funnel, and dried under reduced pressure.
[0054]
The resulting powder was identified as indium oxide (In 2 O 3 ). Moreover, the average particle diameter was 26 nm. As the organic component content of the metal oxide component was 96.6% by weight, signals of methylene and methyl groups of the alkyl chain were observed from NMR to 0.8 to 1.6 ppm.
[0055]
Example 5
Zinc decanoate (C 9 H 19 COO) 2 Zn (10 g) was placed as a solid in a four-necked flask and gradually heated to 320 ° C. while supplying air. After holding at 320 ° C. for 8 hours, it was allowed to cool. The produced powder was repeatedly washed with methanol, filtered off with a Kiriyama funnel, and dried under reduced pressure.
[0056]
The obtained powder was identified as zinc oxide (ZnO) from powder X-ray diffraction analysis. The average particle size was 85 nm. The content of the metal oxide component was 95.1% by weight. Since signals of methylene and methyl groups in the alkyl chain were observed from 0.5 to 1.5 ppm in NMR, it was found that they coexist as organic components.
[Brief description of the drawings]
1 shows the results of powder X-ray diffraction analysis of the powder obtained in Example 1. FIG.
FIG. 2 is an image diagram showing the observation results of the powder obtained in Example 1 by TEM.
3 shows the results of a powder X-ray diffraction analysis of the powder obtained in Example 3. FIG.
4 is an image view showing the observation results of the powder obtained in Example 3 by TEM. FIG.

Claims (4)

金属酸化物超微粒子からなる粉末の製造方法であって、粉末状又は液状の金属有機化合物を、酸化性雰囲気下において、その金属有機化合物の有機質成分の分解開始温度以上、かつ、400℃未満の温度で加熱し、金属酸化物及び有機成分を含有し、前記金属酸化物を50〜95重量%含有する微粒子を得ることを特徴とする方法 A method for producing a powder comprising ultrafine metal oxide particles, wherein a powdered or liquid metal organic compound is heated in an oxidizing atmosphere to a temperature not less than the decomposition start temperature of the organic component of the metal organic compound and less than 400 ° C. method was heated at a temperature, containing a metal oxide and an organic component, characterized in that said metal oxide to obtain a fine particle containing 50 to 95 wt%. 加熱温度が200℃以上400℃未満である、請求項1記載の製造方法。The manufacturing method of Claim 1 whose heating temperature is 200 degreeC or more and less than 400 degreeC. 金属有機化合物が、脂肪酸の金属塩である請求項1又は2に記載の製造方法。The method according to claim 1 or 2, wherein the metal organic compound is a metal salt of a fatty acid. 脂肪酸の炭素数が5〜30である請求項3記載の製造方法。The method according to claim 3, wherein the fatty acid has 5 to 30 carbon atoms.
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US20090264668A1 (en) * 2006-07-31 2009-10-22 Shuzo Tokumitsu Method for production of fineparticle and method for production of indium organocarboxylate
JP5760199B2 (en) * 2012-11-23 2015-08-05 地方独立行政法人 大阪市立工業研究所 Infrared shielding transparent film

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