JP2007239053A - Method for producing alloy nanoparticle and hydrogen storage alloy - Google Patents
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Abstract
Description
本発明は、合金ナノ粒子の製造方法に関し、さらに、この方法により製造が可能となった新たな水素吸蔵合金に関する。 The present invention relates to a method for producing alloy nanoparticles, and further relates to a new hydrogen storage alloy that can be produced by this method.
水素は、燃焼後の生成物が水であるために環境負荷が小さく、今後の主要燃料として期待されている。水素の貯蔵には、水素を可逆的に吸収/放出する水素吸蔵合金が必要となる。パラジウム(Pd)は、水素吸蔵特性を有し、ロジウム(Rh)との合金化によってその水素吸蔵量が増大することが知られている。 Hydrogen has a low environmental impact because the product after combustion is water, and is expected as a future main fuel. Storage of hydrogen requires a hydrogen storage alloy that reversibly absorbs / releases hydrogen. Palladium (Pd) has a hydrogen storage property, and it is known that the hydrogen storage amount increases by alloying with rhodium (Rh).
本発明者は、先に新たな合金ナノ粒子の製造方法を提案した(特許文献1)。この製造方法は、アルコール還元法により得たコア・シェル型構造を有するナノ粒子に水素吸収/放出サイクルを適用することにより、ナノ粒子の構造をコア・シェル型から固溶体型へと変化させるものである。コア・シェル型構造を有するナノ粒子は、まず、コアとなる金属ナノ粒子(特許文献1の実施例ではPdナノ粒子)をアルコール還元法により形成し、次いでこの金属ナノ粒子の表面にシェルとなる金属(同実施例では白金(Pt)シェル)を析出させることにより作製される。 The inventor previously proposed a new method for producing alloy nanoparticles (Patent Document 1). This production method changes the nanoparticle structure from the core-shell type to the solid solution type by applying a hydrogen absorption / release cycle to the nanoparticles having a core-shell type structure obtained by the alcohol reduction method. is there. The nanoparticles having a core-shell structure are formed by first forming metal nanoparticles as cores (Pd nanoparticles in the examples of Patent Document 1) by an alcohol reduction method, and then forming a shell on the surface of the metal nanoparticles. It is produced by depositing metal (in this example, platinum (Pt) shell).
アルコール還元法によるコア・シェル型のナノ粒子の作製は、種々の金属について試行されている(特許文献2;特に[0003][0004])。特許文献2によると、アルコール還元法により、塩化パラジウムと塩化白金とを同時還元すると、PtからなるコアとPdからなるシェルとを有するナノ粒子が形成される([0003])。また、アルコール還元法による同時還元により、金(Au)からなるコアとPtからなるシェルとを有するナノ粒子を得ることもできる([0004])。アルコール還元法に用いるポリビニルピロリドン(PVP)が金よりも白金と強い相互作用をもつために、AuとPtとを同時に還元しても、AuがPtよりも先に還元され、Auコア・Ptシェル構造が生成する。 Preparation of core-shell type nanoparticles by the alcohol reduction method has been tried for various metals (Patent Document 2; in particular, [0003] [0004]). According to Patent Document 2, when palladium chloride and platinum chloride are simultaneously reduced by an alcohol reduction method, nanoparticles having a core made of Pt and a shell made of Pd are formed ([0003]). In addition, nanoparticles having a core made of gold (Au) and a shell made of Pt can be obtained by simultaneous reduction by an alcohol reduction method ([0004]). Since polyvinylpyrrolidone (PVP) used in the alcohol reduction method has a stronger interaction with platinum than gold, even if Au and Pt are reduced simultaneously, Au is reduced before Pt, and Au core / Pt shell A structure is generated.
アルコール還元法によるPd塩とRh塩との同時還元についても報告がある(非特許文献1)。非特許文献1において得られたナノ粒子のEXAFSによる解析結果を参照すると、Pdの配位数はRhの配位数よりも大きくなっている(Table II−V)。これは、Pdがコアを形成し、Rhがシェルを形成していることを示している。
上記で報告されているナノ粒子は、水素吸蔵合金、触媒等としての応用が期待されている。しかし、特許文献1が開示するように、単一の結晶格子を有する固溶体型のナノ粒子を得るためには、水素吸収/放出サイクルを複数回適用する必要があった。特許文献1によれば、固溶体型のナノ粒子は、コア・シェル型のナノ粒子よりも優れた水素吸蔵特性を有する。したがって、水素吸蔵合金としての使用を考慮すると、ナノ粒子は、製造した段階から固溶体型であることが望ましい。 The nanoparticles reported above are expected to be used as hydrogen storage alloys, catalysts and the like. However, as disclosed in Patent Document 1, in order to obtain solid solution-type nanoparticles having a single crystal lattice, it was necessary to apply a hydrogen absorption / release cycle a plurality of times. According to Patent Document 1, solid solution type nanoparticles have better hydrogen storage properties than core / shell type nanoparticles. Therefore, considering the use as a hydrogen storage alloy, it is desirable that the nanoparticles are of a solid solution type from the stage of production.
水素吸蔵合金以外の用途においても、固溶体型への変換を図るために、コア・シェル型のナノ粒子に水素吸収/放出サイクルを適用するのは煩雑であり、製造コストの上昇をもたらす。 Even in applications other than hydrogen storage alloys, it is complicated to apply a hydrogen absorption / release cycle to core / shell type nanoparticles in order to achieve conversion to a solid solution type, resulting in an increase in manufacturing costs.
また、上記のように、Pd/Rh合金は、Pdよりも水素吸蔵量が大きいが、水素吸収/放出サイクルにより、合金が相分離の傾向を示すという問題があった。相分離すると、Rhとの合金化による水素吸蔵量増大の効果も失われる。Pd/Rh合金には、Rhとの合金化により水素吸蔵圧力が上昇するという問題もある。 In addition, as described above, the Pd / Rh alloy has a larger hydrogen storage capacity than Pd, but there is a problem that the alloy shows a tendency of phase separation due to the hydrogen absorption / release cycle. When phase separation occurs, the effect of increasing the amount of hydrogen occlusion by alloying with Rh is lost. The Pd / Rh alloy also has a problem that the hydrogen storage pressure increases due to alloying with Rh.
本発明の目的は、水素吸収/放出サイクルを適用しなくても、Pd原子とPd以外の金属原子とが固溶して単一種の結晶格子を形成した状態となった合金ナノ粒子を得る、新たな製造方法を提供することにある。また、本発明の別の目的は、水素吸収/放出サイクルを適用しても、相分離しないPd/Rh合金からなる水素吸蔵合金の提供にある。 The object of the present invention is to obtain alloy nanoparticles in which Pd atoms and metal atoms other than Pd are in solid solution to form a single kind of crystal lattice without applying a hydrogen absorption / release cycle. It is to provide a new manufacturing method. Another object of the present invention is to provide a hydrogen storage alloy comprising a Pd / Rh alloy that does not phase separate even when a hydrogen absorption / release cycle is applied.
本発明は、Pd塩と、Rh塩またはAu塩である金属塩と、有機高分子と、多価アルコールとを含む溶液を加熱することにより、Pd塩に含まれるPdイオンと上記金属塩に含まれる金属イオンとを同時に還元し、Pd原子と上記金属イオンに由来する金属原子とが固溶して単一種の結晶格子を形成した合金ナノ粒子を得る、合金ナノ粒子の製造方法を提供する。 The present invention includes a Pd ion contained in a Pd salt and the above metal salt by heating a solution containing a Pd salt, a metal salt that is an Rh salt or an Au salt, an organic polymer, and a polyhydric alcohol. A method for producing alloy nanoparticles is provided in which metal nanoparticles are simultaneously reduced to obtain alloy nanoparticles in which a Pd atom and a metal atom derived from the metal ion are in solid solution to form a single type of crystal lattice.
本発明は、その別の側面から、PdおよびRhを含む合金ナノ粒子からなり、この合金ナノ粒子においてPdとRhとが単一種の結晶格子を形成し、この合金ナノ粒子に水素吸収/放出サイクルを適用した後にも単一種の結晶格子が維持される水素吸蔵合金を提供する。単一種の結晶格子が維持されるか否かを判断するための水素吸収/放出サイクルは、具体的には、後述する条件での処理(573Kで20気圧(2MPa)の水素雰囲気中に2時間放置し、その後、7×10-4Paにまで真空引きする処理)とすればよい。 Another aspect of the present invention is an alloy nanoparticle containing Pd and Rh. In this alloy nanoparticle, Pd and Rh form a single kind of crystal lattice, and a hydrogen absorption / release cycle is formed in the alloy nanoparticle. The present invention provides a hydrogen storage alloy in which a single type of crystal lattice is maintained even after application of. Specifically, a hydrogen absorption / release cycle for determining whether or not a single type of crystal lattice is maintained is specifically a treatment under the conditions described later (2 hours in a hydrogen atmosphere at 573 K and 20 atm (2 MPa)). And then evacuating to 7 × 10 −4 Pa).
本発明によれば、水素吸収/放出サイクルを適用しなくても、単一種の結晶格子が内在する(換言すれば完全に固溶体型となった)合金ナノ粒子を得ることができる。多価アルコールは、エタノールに代表される一価のアルコールに比べて強い還元作用を有すると考えられる。この強い還元作用をパラジウムイオンと特定の金属イオンとの同時還元に適用すると、水素吸収/放出サイクルを適用しなくても、完全に固溶体型となった合金ナノ粒子を得ることができる。 According to the present invention, alloy nanoparticles having a single type of crystal lattice (in other words, completely solid solution type) can be obtained without applying a hydrogen absorption / release cycle. Polyhydric alcohols are considered to have a stronger reducing action than monohydric alcohols typified by ethanol. When this strong reduction action is applied to the simultaneous reduction of palladium ions and specific metal ions, alloy nanoparticles in a completely solid solution type can be obtained without applying a hydrogen absorption / release cycle.
また、本発明によれば、水素吸収/放出サイクルを適用した後にも、相分離せずに合金化の効果が維持されたPd/Rh合金からなる水素吸蔵合金を提供できる。 Further, according to the present invention, it is possible to provide a hydrogen storage alloy composed of a Pd / Rh alloy that maintains the effect of alloying without phase separation even after applying a hydrogen absorption / release cycle.
多価アルコールの強い相互作用を適用しても、例えばイリジウム(Ir)のようにPdと分離する傾向が強い金属は、Pdと固溶体型の合金ナノ粒子を形成することができない。上述のRh等の金属は、Pdとの相溶性がある程度高いために、多価アルコールの強い還元力を作用させると固溶体型の合金ナノ粒子が形成されると考えられる。 Even if a strong interaction of polyhydric alcohol is applied, a metal having a strong tendency to separate from Pd, such as iridium (Ir), cannot form solid solution type alloy nanoparticles with Pd. The metals such as Rh described above have a high compatibility with Pd to some extent, and it is considered that solid solution type alloy nanoparticles are formed when the strong reducing power of polyhydric alcohol is applied.
本発明による合金ナノ粒子は、いわゆるアルコール還元法により製造される。アルコール還元法は、従来から知られているように、有機高分子の存在下、アルコールを含む溶液中で金属イオンを還元するナノ粒子の製造方法である。 The alloy nanoparticles according to the present invention are produced by a so-called alcohol reduction method. As conventionally known, the alcohol reduction method is a method for producing nanoparticles in which metal ions are reduced in a solution containing alcohol in the presence of an organic polymer.
有機高分子としては、水溶性のポリマーが好ましく、具体的にはポリビニルピロリドン(PVP)のような環状アミド構造を有するポリマーが好適であるが、これに限らず、目的とする金属粒子の種類等に応じ、例えばポリビニルアルコール、ポリビニルエーテル、ポリアクリレート、ポリアクリロニトリル等を用いてもよい。 As the organic polymer, a water-soluble polymer is preferable, and specifically, a polymer having a cyclic amide structure such as polyvinylpyrrolidone (PVP) is preferable. For example, polyvinyl alcohol, polyvinyl ether, polyacrylate, polyacrylonitrile, or the like may be used.
アルコールは、溶液中で還元剤として作用する。本発明では、エチレングリコールに代表される多価アルコールを用いる。多価アルコールは、一価のアルコールよりも高い還元作用を発揮することができる。多価アルコールとしては、エチレングリコールとともに、プロピレングリコール、グリセリン等が挙げられる。 Alcohol acts as a reducing agent in solution. In the present invention, a polyhydric alcohol typified by ethylene glycol is used. Polyhydric alcohols can exhibit a higher reducing action than monohydric alcohols. Examples of the polyhydric alcohol include ethylene glycol, propylene glycol, glycerin and the like.
金属イオンを還元するために溶液を加熱する温度は、90℃以上、例えば90℃〜198℃、さらには90℃〜150℃が適当である。また、同時還元によって完全に固溶体型である合金ナノ粒子を得るためには、できるだけ短時間で金属イオンを還元することが望ましい。上記温度で加熱する時間は、例えば1.5時間以内、好ましくは1時間以内、である。短時間で加熱するほうが完全に固溶体型となった合金ナノ粒子が得られやすい傾向があるためである。 The temperature at which the solution is heated to reduce the metal ions is 90 ° C or higher, for example, 90 ° C to 198 ° C, more preferably 90 ° C to 150 ° C. In order to obtain alloy nanoparticles that are completely solid solution by simultaneous reduction, it is desirable to reduce metal ions in as short a time as possible. The time for heating at the above temperature is, for example, within 1.5 hours, preferably within 1 hour. This is because heating in a short time tends to provide alloy nanoparticles that are completely in a solid solution type.
溶液中における有機高分子の量を相対的に増やすと、析出するナノ粒子の粒径は小さくなるため、これを利用すればナノ粒子の粒径を制御できる。添加する金属塩の濃度を調整することによっても、析出する金属の量、ひいてはナノ粒子の粒径を制御できる。得られる粒子の組成の均一性も高い。このように、アルコール還元法は、粒径等の制御性に優れており、ナノ粒子の製造方法として適している。 When the amount of the organic polymer in the solution is relatively increased, the particle size of the deposited nanoparticles becomes small, and this can be used to control the particle size of the nanoparticles. By adjusting the concentration of the metal salt to be added, it is possible to control the amount of the deposited metal and thus the particle size of the nanoparticles. The uniformity of the composition of the obtained particles is also high. Thus, the alcohol reduction method is excellent in controllability such as particle size, and is suitable as a method for producing nanoparticles.
本発明による合金ナノ粒子の粒径は、特に制限はないが、100nm以下、例えば0.5nm〜100nm、さらには1nm〜100nm、特に2nm〜50nm、とりわけ2nm〜20nmが好適であり、10nm以下であってもよい。 The particle diameter of the alloy nanoparticles according to the present invention is not particularly limited, but is preferably 100 nm or less, such as 0.5 nm to 100 nm, more preferably 1 nm to 100 nm, particularly 2 nm to 50 nm, especially 2 nm to 20 nm, preferably 10 nm or less. There may be.
本発明により得られる合金ナノ粒子は、特に粒径が小さい場合には、有機高分子で被覆された状態で使用することが好ましい。この状態は微粒子の酸化防止に有効である。保護剤となる有機高分子は、特に制限されず、アルコール還元法で用いる各種ポリマーをそのまま用いればよい。 The alloy nanoparticles obtained by the present invention are preferably used in a state of being coated with an organic polymer, particularly when the particle size is small. This state is effective for preventing oxidation of fine particles. The organic polymer used as the protective agent is not particularly limited, and various polymers used in the alcohol reduction method may be used as they are.
本発明による水素吸蔵合金は、本発明の製造方法において金属塩としてRh塩を用いて得たものであってもよい。この水素吸蔵合金は、水素吸収/放出サイクルの適用前から、PdとRhとが原子レベルで固溶したものとなる。 The hydrogen storage alloy according to the present invention may be obtained by using an Rh salt as a metal salt in the production method of the present invention. In this hydrogen storage alloy, Pd and Rh are in solid solution at the atomic level before application of the hydrogen absorption / release cycle.
以下、実施例により本発明をさらに具体的に説明するが、以下の実施例は、本欄における上記記載と同様、本発明の実施形態の例示に過ぎず、本発明を限定するものではない。 EXAMPLES Hereinafter, the present invention will be described more specifically with reference to examples. However, the following examples are only examples of the embodiments of the present invention, as described above in this section, and do not limit the present invention.
(Pd/Rh合金ナノ粒子の合成)
PVP0.111g(1mmol)をエチレングリコール20mlに添加し、マグネチックスターラーにより撹拌し溶解して、PVPエチレングリコール溶液を調製した。一方で、硝酸パラジウム(II) n水和物0.0133g(水を39.9重量%含む)(0.05mmol)と塩化ロジウム(III)三水和物 0.0132gとを水2mlに溶解させて、Pd−Rh混合水溶液を得た。Pd−Rh混合水溶液をPVPエチレングリコール溶液に添加し、加熱を開始した。温度が95 ℃に至った段階で1時間撹拌し、黒褐色溶液を得た。
(Synthesis of Pd / Rh alloy nanoparticles)
0.111 g (1 mmol) of PVP was added to 20 ml of ethylene glycol and dissolved by stirring with a magnetic stirrer to prepare a PVP ethylene glycol solution. Meanwhile, 0.0133 g of palladium nitrate (II) n hydrate (containing 39.9% by weight of water) (0.05 mmol) and 0.0132 g of rhodium (III) chloride trihydrate were dissolved in 2 ml of water. Thus, a Pd—Rh mixed aqueous solution was obtained. The Pd—Rh mixed aqueous solution was added to the PVP ethylene glycol solution, and heating was started. When the temperature reached 95 ° C., the mixture was stirred for 1 hour to obtain a dark brown solution.
この溶液が室温に戻った後、遠心分離用チューブに移し、ジエチルエーテル、アセトンを添加し(試料溶液:ジエチルエーテル:アセトン=5:4:5、体積比)、この溶液を遠心分離した。その後、上澄みを捨て、得られた黒色沈殿をエタノール5mlに溶解させた。さらにジエチルエーテルを加え、濁った溶液を再び遠心分離した。再び上澄みを捨て、アセトン5ml、ジエチルエーテル15mlを加え、さらに遠心分離した。こうして得た沈殿をアセトンで3回洗浄し、真空引きし、乾固させ、Pd/Rh合金ナノ粒子を得た。 After this solution returned to room temperature, it was transferred to a centrifuge tube, diethyl ether and acetone were added (sample solution: diethyl ether: acetone = 5: 4: 5, volume ratio), and this solution was centrifuged. Thereafter, the supernatant was discarded, and the resulting black precipitate was dissolved in 5 ml of ethanol. Further diethyl ether was added and the cloudy solution was centrifuged again. The supernatant was discarded again, 5 ml of acetone and 15 ml of diethyl ether were added, and the mixture was further centrifuged. The precipitate thus obtained was washed with acetone three times, vacuumed and dried to obtain Pd / Rh alloy nanoparticles.
(透過型電子顕微鏡(TEM)を用いた観察)
Pd/Rh合金ナノ粒子をTEM観察した。TEM観察は、加速電圧200kV、倍率10万倍として行った。平均粒径は、TEM写真中の任意エリアから約300個の粒子を選出して直径(粒径)を測定した。TEM写真を図1に、粒径の測定結果を図2に示す。図2に示した統計の結果から、平均粒径および標準偏差を算出した。Pd/Rh合金ナノ粒子の平均粒径は4.0nm、標準偏差は0.9nmであった。
(Observation using transmission electron microscope (TEM))
Pd / Rh alloy nanoparticles were observed by TEM. The TEM observation was performed with an acceleration voltage of 200 kV and a magnification of 100,000 times. For the average particle diameter, about 300 particles were selected from an arbitrary area in the TEM photograph, and the diameter (particle diameter) was measured. A TEM photograph is shown in FIG. 1, and the measurement results of the particle diameter are shown in FIG. From the statistical results shown in FIG. 2, the average particle size and standard deviation were calculated. The average particle diameter of the Pd / Rh alloy nanoparticles was 4.0 nm, and the standard deviation was 0.9 nm.
(粉末X線回折による分析)
0.5mmφのガラスキャピラリーに上記で得たPd/Rh合金ナノ粒子を封入した。測定は波長0.068812nmの放射光を用いて行った。図3に、Pdナノ粒子、Rhナノ粒子とともに、Pd/Rh合金ナノ粒子についての測定結果を示す。この結果より、Pd/Rh合金ナノ粒子には単一の面心立方(fcc)格子が内在することが確認できた。なお、Pdナノ粒子およびRhナノ粒子も、上記と同様のアルコール還元法により得たものを用いた。
(Analysis by powder X-ray diffraction)
The Pd / Rh alloy nanoparticles obtained above were encapsulated in a 0.5 mmφ glass capillary. The measurement was performed using synchrotron radiation having a wavelength of 0.068812 nm. FIG. 3 shows the measurement results for Pd / Rh alloy nanoparticles together with Pd nanoparticles and Rh nanoparticles. From this result, it was confirmed that the Pd / Rh alloy nanoparticles had a single face-centered cubic (fcc) lattice. Pd nanoparticles and Rh nanoparticles were also obtained by the same alcohol reduction method as described above.
さらに、水素吸収/放出サイクルに伴う構造の変化を観察するため、上記で得たPd/Rh合金ナノ粒子を、573Kで2MPaの水素雰囲気下に2時間保持し、その後、7×10-4Paにまで真空引きして、上記サイクルを1回適用した。水素吸収/放出サイクル適用前後のX線回折パターンを図4に示す。図4に示したように、水素吸収/放出サイクルの適用後、Pd/Rh合金ナノ粒子に相分離の傾向は見られず、X線回折パターンに現れたピークはむしろ鋭くなった。 Furthermore, in order to observe the structural change accompanying the hydrogen absorption / release cycle, the Pd / Rh alloy nanoparticles obtained above were held at 573 K in a 2 MPa hydrogen atmosphere for 2 hours, and then 7 × 10 −4 Pa. And the above cycle was applied once. The X-ray diffraction patterns before and after application of the hydrogen absorption / release cycle are shown in FIG. As shown in FIG. 4, after application of the hydrogen absorption / release cycle, the Pd / Rh alloy nanoparticles showed no phase separation tendency and the peaks that appeared in the X-ray diffraction pattern were rather sharp.
比較のために、バルクのPd/Rh合金に対しても、上記と同じ条件で水素吸収/放出サイクルを1回適用した。このサイクルの適用前後のX線回折パターンを図5に示す。バルク合金では水素処理によってピークが分裂したことがわかる(例えば図5に矢印で示したピーク)。このピークの分裂はPdとRhとが相分離したことを示している。 For comparison, a hydrogen absorption / release cycle was applied once to the bulk Pd / Rh alloy under the same conditions as described above. X-ray diffraction patterns before and after application of this cycle are shown in FIG. In the bulk alloy, it can be seen that the peak was split by hydrogen treatment (for example, the peak indicated by the arrow in FIG. 5). This peak splitting indicates that Pd and Rh are phase separated.
このように、バルク合金では、水素放出/吸収サイクルの適用によって合金が相分離する傾向を示すが、合金ナノ粒子では、Rh添加の効果が同サイクルの適用によっても失われないことが確認できた。 As described above, in the bulk alloy, the alloy tends to phase-separate by application of the hydrogen release / absorption cycle, but in the alloy nanoparticles, it was confirmed that the effect of Rh addition was not lost even by application of the same cycle. .
(水素吸蔵能力の確認)
上記で得たPd/Rh合金ナノ粒子について、PCT(Hydrogen Pressure -Composition-Isotherms)曲線を測定した。測定には、PCT自動特性測定装置(鈴木商館製)を用いた。結果を図6に示す。測定温度は303Kとした。
(Confirmation of hydrogen storage capacity)
A PCT (Hydrogen Pressure-Composition-Isotherms) curve was measured for the Pd / Rh alloy nanoparticles obtained above. For the measurement, a PCT automatic characteristic measuring device (manufactured by Suzuki Shokan) was used. The results are shown in FIG. The measurement temperature was 303K.
熔融急冷法等で作製したバルクのPd/Rh合金箔の場合、Rhの添加に伴って水素吸蔵圧力が大幅に上昇することが知られている。しかし、図6に示したように、合金ナノ粒子では、0.1MPa(760Torr)以下の水素圧力でプラトー領域が現れている。図6に示したように、Pd/Rh合金ナノ粒子は、水素圧力1MPaにおいてもまだプラトー領域にあるため、高圧下ではさらに大きな水素吸蔵量を示すと考えられる。 In the case of a bulk Pd / Rh alloy foil produced by a melt quenching method or the like, it is known that the hydrogen occlusion pressure significantly increases with the addition of Rh. However, as shown in FIG. 6, in the alloy nanoparticles, a plateau region appears at a hydrogen pressure of 0.1 MPa (760 Torr) or less. As shown in FIG. 6, since the Pd / Rh alloy nanoparticles are still in the plateau region even at a hydrogen pressure of 1 MPa, it is considered that the hydrogen storage amount is larger under high pressure.
本発明の製造方法によれば、水素吸収/放出サイクルを適用しなくても、複数種の金属原子が原子レベルで合金化されたナノ粒子を得ることができる。本発明は、導電性ペースト、触媒、水素吸蔵合金の分野、において利用価値が高い。さらに、本発明は、水素吸収/放出サイクルを適用しても相分離する傾向を示さないPd/Rh合金を提供するものとして、水素吸蔵合金の分野において多大な利用価値を有する。 According to the production method of the present invention, nanoparticles in which a plurality of types of metal atoms are alloyed at the atomic level can be obtained without applying a hydrogen absorption / release cycle. The present invention has high utility value in the fields of conductive pastes, catalysts, and hydrogen storage alloys. Furthermore, the present invention has great utility in the field of hydrogen storage alloys as providing a Pd / Rh alloy that does not show a tendency to phase separate even when applied with a hydrogen absorption / release cycle.
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Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
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WO2010122811A1 (en) * | 2009-04-24 | 2010-10-28 | 独立行政法人科学技術振興機構 | Fine solid solution alloy particles and method for producing same |
CN103370153A (en) * | 2011-03-04 | 2013-10-23 | 丰田自动车株式会社 | Metal particles, catalyst for exhaust gas purification containing same, and production method therefor |
WO2017150580A1 (en) * | 2016-03-01 | 2017-09-08 | 国立大学法人京都大学 | Ru Cu SOLID SOLUTION NANOPARTICLES, PRODUCTION METHOD THEREFOR, AND CATALYST |
CN113020615A (en) * | 2021-03-03 | 2021-06-25 | 中海油(山西)贵金属有限公司 | Method for preparing high-purity rhodium powder by using rhodium trichloride |
CN114682791A (en) * | 2022-03-31 | 2022-07-01 | 长沙新材料产业研究院有限公司 | Gold nanoparticle dispersion, gold nanoparticles and preparation method thereof |
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Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2877410B2 (en) * | 1990-01-19 | 1999-03-31 | 田中貴金属工業株式会社 | Preparation method of noble metal fine particles |
JP2003226901A (en) * | 2002-02-05 | 2003-08-15 | Hitachi Maxell Ltd | Binary alloy fine particle and production method therefor |
JP2005272970A (en) * | 2004-03-25 | 2005-10-06 | Kyushu Univ | Alloy particle and production method therefor |
JP2008525638A (en) * | 2004-12-22 | 2008-07-17 | ブルックヘヴン サイエンス アソシエイツ | Metal deposition on palladium and palladium alloy particles induced by hydrogen absorption |
-
2006
- 2006-03-09 JP JP2006064810A patent/JP4257981B2/en active Active
Patent Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2877410B2 (en) * | 1990-01-19 | 1999-03-31 | 田中貴金属工業株式会社 | Preparation method of noble metal fine particles |
JP2003226901A (en) * | 2002-02-05 | 2003-08-15 | Hitachi Maxell Ltd | Binary alloy fine particle and production method therefor |
JP2005272970A (en) * | 2004-03-25 | 2005-10-06 | Kyushu Univ | Alloy particle and production method therefor |
JP2008525638A (en) * | 2004-12-22 | 2008-07-17 | ブルックヘヴン サイエンス アソシエイツ | Metal deposition on palladium and palladium alloy particles induced by hydrogen absorption |
Cited By (12)
Publication number | Priority date | Publication date | Assignee | Title |
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WO2010122811A1 (en) * | 2009-04-24 | 2010-10-28 | 独立行政法人科学技術振興機構 | Fine solid solution alloy particles and method for producing same |
CN102458727A (en) * | 2009-04-24 | 2012-05-16 | 独立行政法人科学技术振兴机构 | Fine solid solution alloy particles and method for producing same |
JPWO2010122811A1 (en) * | 2009-04-24 | 2012-10-25 | 独立行政法人科学技術振興機構 | Solid solution type alloy fine particles and method for producing the same |
JP5639045B2 (en) * | 2009-04-24 | 2014-12-10 | 独立行政法人科学技術振興機構 | Method for producing fine particle group comprising solid solution type alloy fine particles |
JP2015034347A (en) * | 2009-04-24 | 2015-02-19 | 独立行政法人科学技術振興機構 | Solid solution type alloy fine particles, and method for manufacturing the same |
US9273378B2 (en) | 2009-04-24 | 2016-03-01 | Japan Science And Technology Agency | Fine solid solution alloy particles and method for producing same |
US9540712B2 (en) | 2009-04-24 | 2017-01-10 | Japan Science And Technology Agency | Fine solid solution alloy particles and method for producing same |
CN103370153A (en) * | 2011-03-04 | 2013-10-23 | 丰田自动车株式会社 | Metal particles, catalyst for exhaust gas purification containing same, and production method therefor |
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JPWO2017150580A1 (en) * | 2016-03-01 | 2019-01-31 | 国立大学法人京都大学 | RuCu solid solution nanoparticles, production method thereof and catalyst |
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