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TWI422431B - Preparation method of cobalt composite catalyst - Google Patents

Preparation method of cobalt composite catalyst Download PDF

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TWI422431B
TWI422431B TW100125878A TW100125878A TWI422431B TW I422431 B TWI422431 B TW I422431B TW 100125878 A TW100125878 A TW 100125878A TW 100125878 A TW100125878 A TW 100125878A TW I422431 B TWI422431 B TW I422431B
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cobalt
iron
composite catalyst
solution
cobalt composite
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TW201304862A (en
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Huei Mei Tsai
Su Ming Chang
Jung He Kuo
Chi Wen Tsai
Ru Shi Liu
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Chung Shan Inst Of Science
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一種鈷複合觸媒製備方法 Preparation method of cobalt composite catalyst

本發明係屬於一種觸媒之製備方法,特別是指一種用於化學儲氫材料,利用鈷金屬製成複合觸媒進行催化產氫之方法。 The invention belongs to a preparation method of a catalyst, in particular to a method for catalytic hydrogen production by using a cobalt metal as a composite catalyst for chemical hydrogen storage materials.

氫能為多種考量替代能源之一,為燃料電池中最乾淨之燃料,於轉化過程不產生溫室氣體或其它有害物,零排放為其最大特性,因此是為最具開發價值之能源。目前已開發之幾種儲存氫氣之方式其中化學氫儲存方式極具發展潛力。 Hydrogen energy is one of the most considerable alternative energy sources. It is the cleanest fuel in fuel cells. It does not produce greenhouse gases or other harmful substances in the conversion process. Zero emission is its most characteristic, so it is the most valuable energy. Several ways of storing hydrogen have been developed, among which the chemical hydrogen storage method has great development potential.

於化學氫系統中,實際應用之材料選擇必須考慮四大部分:a.材料價格、b.安全性、c.材料效能、d.穩定性。硼氫化鈉於各項之表現皆符合要求,其應用於燃料電池供氫系統之優點如下: In the chemical hydrogen system, the material selection for practical application must consider four major parts: a. material price, b. safety, c. material efficiency, d. stability. The performance of sodium borohydride in all of them meets the requirements. The advantages of applying it to the fuel cell hydrogen supply system are as follows:

1. NaBH4溶解度高,易配製成溶液。 1. NaBH 4 has high solubility and is easy to prepare into a solution.

2. NaBH4溶液於鹼性條件下較安定,可保存數個月亦不變質。 2. The NaBH 4 solution is stable under alkaline conditions and can be stored for several months without deterioration.

3. NaBH4溶液生成氫氣之反應相較於其他化學氫之反應具較高儲氫效率,此反應之反應速率易控制。 3. The reaction of hydrogen in NaBH 4 solution has higher hydrogen storage efficiency than the reaction of other chemical hydrogen, and the reaction rate of this reaction is easy to control.

4. 此反應唯一副產物(NaBO2)溶解度高,易溶於水中,故可直接得到乾淨之氫氣,且NaBO2可循環再生成NaBH44. The only by-product (NaBO 2 ) of this reaction has high solubility and is easily soluble in water, so that clean hydrogen can be directly obtained, and NaBO 2 can be recycled to form NaBH 4 .

5. 於特定之催化劑反應下,NaBH4短時間內可生成大量之氫氣。氣體生成物為氫氣與水蒸氣,氫氣呈潤濕態,可直接供給燃料電池反應。 5. Under the specific catalyst reaction, NaBH 4 can generate a large amount of hydrogen in a short time. The gas product is hydrogen and water vapor, and the hydrogen gas is in a wet state and can be directly supplied to the fuel cell for reaction.

6. 即使於0℃條件下,仍可生成氫氣。 6. Hydrogen can be produced even at 0 °C.

硼氫化鈉配製成鹼性溶液其具上述之優點,故硼氫化鈉乃是最被廣為研究之化學氫。2002年千禧電池公司成功開發以硼氫化鈉化學氫為原料,搭配系統之設計,實際供氫於裝載燃料電池之汽車。因此研發利用觸媒材料促使硼氫化鈉與水反應產生氫氣之方法與技術,其所衍生的產業價值將是無可限量。 Sodium borohydride is the most widely studied chemical hydrogen since it is formulated into an alkaline solution with the above advantages. In 2002, Millennium Battery Company successfully developed sodium borohydride chemical hydrogen as raw material, and matched the design of the system to actually supply hydrogen to the fuel cell. Therefore, the development of methods and technologies for the use of catalytic materials to promote the reaction of sodium borohydride with water to produce hydrogen, the industrial value derived from it will be unlimited.

習用奈米鈷金屬產氫觸媒,如中國青島科技大學所揭示[Int.J. Hydrogen Energy 33,7371(2008)],其利用硝酸[HNO3]修飾活性碳,使其表面帶有具親水性之官能基。接著含浸前驅物硝酸鈷溶液,由於親水性官能基之增加,而使得活性碳能抓取更多的金屬鈷,具催化能力之活性位置增加。然而因其需使用活性碳,故需另外使用載體。再者活性碳尚須經表面修飾官能基,才能提高金屬含浸於活性碳表面之數量,仍有其製程上之限制,而本發明之載體鐵不需進行表面修飾而簡化了觸媒之製程。再者,於[Fuel Cells 10,132(2010)]文獻中,則首次揭示以鈷及鐵雙金屬所合成之奈米複合觸媒應用於硼氫化鈉產氫反應。鈷與鐵莫耳數比達17比3時,可有最大活性,其價格雖因鐵之取代而降低,然製程簡化及價格仍有其進一步下降之空間。藉此,本發明合成以更多鐵取代鈷金屬之奈米複合觸媒,達到成本降低之商業應用價值。 Hydrogen-catalyzed by nano-cobalt metal, as revealed by Qingdao University of Science and Technology, China [ Int. J. Hydrogen Energy 33 , 7731 (2008)], which uses activated carbon [HNO 3 ] to modify activated carbon to make its surface hydrophilic. Functionality of sex. Next, the precursor cobalt nitrate solution is impregnated, and due to the increase of the hydrophilic functional group, the activated carbon can capture more metal cobalt, and the active position of the catalytic ability increases. However, since it requires the use of activated carbon, it is necessary to additionally use a carrier. Furthermore, the activated carbon still needs to be surface-modified functional groups to increase the amount of metal impregnated on the surface of the activated carbon, and there are still limitations in its process. However, the carrier iron of the present invention does not require surface modification to simplify the process of the catalyst. Furthermore, in [ Factor Cells 10 , 132 (2010)], it was first revealed that a nanocomposite catalyst synthesized from cobalt and an iron bimetal is used for the hydrogen production reaction of sodium borohydride. When the cobalt to iron molar ratio is 17 to 3, it has the maximum activity, and its price is reduced by the substitution of iron. However, the process simplification and price still have room for further decline. Thereby, the present invention synthesizes a nanocomposite catalyst which replaces cobalt metal with more iron, and achieves commercial value of cost reduction.

鑒於上述習知技術之缺點,本發明主要目的在於提供一種鈷複合觸媒之製備方法,利用含鐵化合物、含鈷化合物及 還原劑製成產氫鈷複合奈米觸媒,藉以達到製程簡化及成本降低之目的。 In view of the above disadvantages of the prior art, the main object of the present invention is to provide a method for preparing a cobalt composite catalyst, which utilizes an iron-containing compound, a cobalt-containing compound, and The reducing agent is made into a hydrogen-producing cobalt composite nanocatalyst to achieve process simplification and cost reduction.

為了達到上述目的本發明提供一種鈷複合觸媒製備方法,其步驟係包括提供一含鐵化合物及一含鈷化合物,將該含鐵化合物加入一還原劑後再將含鈷化合物加入該含鐵溶液中而得一鐵鈷混合液,而後提供一還原劑加入該鐵鈷混合液形成鈷複合觸媒。而加入還原劑之目的主要是用來將觸媒中的金屬離子還原成金屬原子,形成奈米級粒子。本發明之特點在於不使用任何貴重金屬,而改以鈷金屬為活性中心,並利用鐵作為載體提高鈷粒子之活性面積,進一步達到簡化製程及降低成本之目的。 In order to achieve the above object, the present invention provides a method for preparing a cobalt composite catalyst, which comprises the steps of providing an iron-containing compound and a cobalt-containing compound, adding the iron-containing compound to a reducing agent, and then adding the cobalt-containing compound to the iron-containing solution. An iron-cobalt mixture is obtained in the middle, and then a reducing agent is added to the iron-cobalt mixture to form a cobalt composite catalyst. The purpose of adding the reducing agent is mainly to reduce the metal ions in the catalyst to metal atoms to form nano-sized particles. The invention is characterized in that instead of using any precious metal, cobalt metal is used as an active center, and iron is used as a carrier to increase the active area of the cobalt particles, thereby further simplifying the process and reducing the cost.

於本發明之實施例中,亦將說明產氫觸媒之成分及製備方法。此觸媒係為以鈷為活性中心支撐於鐵粒子上之複合奈米粒子,其中含鐵化合物係以氯化鐵(FeCl3‧6H2O)為前驅物;含鈷化合物係以氯化鈷(CoCl2‧6H2O)為前驅物,並以硼氫化鈉(NaBH4)為還原劑所合成。 In the examples of the present invention, the components of the hydrogen-producing catalyst and the preparation method thereof will also be explained. The catalyst is a composite nanoparticle supported on iron particles with cobalt as an active center, wherein the iron-containing compound is a ferric chloride (FeCl 3 ‧6H 2 O) as a precursor; the cobalt-containing compound is a cobalt chloride (CoCl 2 ‧6H 2 O) is a precursor and is synthesized using sodium borohydride (NaBH 4 ) as a reducing agent.

此產氫活性測試乃利用氫氣於水中溶解度不大,而可使用排水集氣法收集氫氣,並量測其生成量與相對時間而得知產氫速率,此法可比較不同觸媒之產氫速率。因硼氫化鈉與水接觸極易反應,故添加氫氧化鈉於溶液中扮演穩定劑之角色,可減緩硼氫化鈉與水反應之速率,延長硼氫化鈉溶液之儲存壽命。 The hydrogen production activity test uses hydrogen to have little solubility in water, and the hydrogen collection method can be used to collect hydrogen gas, and the amount of production and relative time can be measured to know the hydrogen production rate. This method can compare hydrogen production by different catalysts. rate. Since sodium borohydride is highly reactive with water, the addition of sodium hydroxide acts as a stabilizer in the solution, which slows the reaction rate of sodium borohydride with water and prolongs the storage life of the sodium borohydride solution.

以上之概述與接下來的詳細說明及附圖,皆是為了能進 一步說明本發明達到預定目的所採取的方式、手段及功效。而有關本發明的其它目的及優點,將在後續的說明及圖示中加以闡述。 The above summary and the following detailed description and drawings are for the purpose of The manner, means and efficacy of the present invention for achieving the intended purpose are explained in one step. Other objects and advantages of the present invention will be described in the following description and drawings.

以下係藉由特定的具體實例說明本發明之實施方式,熟悉此技藝之人士可由本說明書所揭示之內容輕易地瞭解本發明之其它優點與功效。 The embodiments of the present invention are described below by way of specific examples, and those skilled in the art can readily appreciate the other advantages and advantages of the present invention.

請參閱第1圖所示,本發明係以合成一種鈷複合觸媒製備方法,其步驟係包括:步驟(A):提供一含鐵化合物及一含鈷化合物(S101),以去離子水為溶劑配置成含鐵水溶液及含鈷水溶液;步驟(B):將該含鐵化合物加入一還原劑(S102),此還原環境為中性水相,並於攪拌子轉動下加入該還原劑;步驟(C):將含鈷化合物加入該含鐵溶液中而得一鐵鈷混合液(S103);步驟(D):提供一還原劑加入該鐵鈷混合液而形成鈷複合觸媒(S104),此還原環境為中性水相,並於攪拌子轉動下加入該還原劑。 Referring to Fig. 1, the present invention is a method for preparing a cobalt composite catalyst, the steps of which include: step (A): providing an iron-containing compound and a cobalt-containing compound (S101), using deionized water as The solvent is disposed as an aqueous solution containing iron and a solution containing cobalt; step (B): adding the iron-containing compound to a reducing agent (S102), the reducing environment is a neutral aqueous phase, and the reducing agent is added under rotation of the stirring device; (C): adding a cobalt-containing compound to the iron-containing solution to obtain a mixture of iron and cobalt (S103); and (D): providing a reducing agent to the iron-cobalt mixture to form a cobalt composite catalyst (S104), The reducing environment is a neutral aqueous phase, and the reducing agent is added while the stirring is rotating.

其中,為了取出鈷複合觸媒更進一步提出另外三個步驟:步驟(E):係為利用磁性吸附觸媒粉末;步驟(F):利用過濾法過濾出該鈷複合觸媒;步驟(G):將該鈷複合觸媒烘乾進行乾燥處理移除不必要之溶劑,並研磨該觸媒粒子用以平均粒子尺寸。藉此,製備一種用於化學儲氫材料產氫觸媒,以鈷金屬為活性中心,並 利用鐵作為載體提高鈷粒子之活性面積,進一步達到簡化製程及降低成本之目的。 In order to take out the cobalt composite catalyst, another three steps are further proposed: step (E): using magnetic adsorption catalyst powder; step (F): filtering out the cobalt composite catalyst by filtration; step (G) The cobalt composite catalyst is dried and dried to remove unnecessary solvent, and the catalyst particles are ground to average particle size. Thereby, preparing a hydrogen catalyst for chemical hydrogen storage materials, using cobalt metal as an active center, and The use of iron as a carrier to increase the active area of the cobalt particles further simplifies the process and reduces the cost.

實施例一: Embodiment 1:

將0.02M之氯化鐵(FeCl3‧6H2O)溶液100毫升置於反應瓶,以攪拌子於500rpm轉速中,逐滴加入配置好之還原劑硼氫化鈉(NaBH4)溶液,可見到反應瓶中溶液逐漸轉為灰黑色,放置24小時。於上述反應瓶溶液中再加入另一0.02M之氯化鈷(CoCl2‧6H2O)溶液100毫升。在攪拌子轉速為500rpm下,滴入配置好之還原劑硼氫化鈉(NaBH4)溶液,再放置24小時。將此溶液以磁鐵吸住產物灰黑色粉末,此粉末即為觸媒粉末。利用去離子水過濾此觸媒粉末五次,確保雜質洗淨後,烘乾並研磨得細緻黑色觸媒粉末。由X-ray繞射圖(第2圖)知所合成之觸媒為非晶相結構。 100 ml of a 0.02 M ferric chloride (FeCl 3 ‧6H 2 O) solution was placed in a reaction flask, and the prepared reducing agent sodium borohydride (NaBH 4 ) solution was added dropwise at 500 rpm with a stir bar. The solution in the reaction flask was gradually turned grayish black and allowed to stand for 24 hours. Another 100 ml of a 0.02 M cobalt chloride (CoCl 2 ‧6H 2 O) solution was added to the above reaction flask solution. The prepared reducing agent sodium borohydride (NaBH 4 ) solution was dropped at a stirring speed of 500 rpm and allowed to stand for 24 hours. This solution was sucked by a magnet to the product gray-black powder, which was a catalyst powder. The catalyst powder was filtered five times with deionized water to ensure that the impurities were washed, dried and ground to obtain a fine black catalyst powder. The X-ray diffraction pattern (Fig. 2) shows that the catalyst synthesized is an amorphous phase structure.

產氫活性測試方法如下所示:以去離子水配製重量百分濃度5wt%硼氫化鈉(NaBH4)溶液及重量百分濃度5wt%氫氧化鈉(NaOH)溶液,架設產氫裝置,設定恆溫槽溫度於室溫298K下。秤取適當量約10毫克之觸媒置於圓底單頸瓶,爾後注入5wt%硼氫化鈉(NaBH4)溶液及5wt%氫氧化鈉(NaOH)溶液10毫升,此時大量氣泡生成此氣泡即為氫氣,該生成量可經量筒刻度記錄。所測得知鐵鈷核殼觸媒奈米粒子平均產氫速率為2200(ml/g.min),若單純與鈷金屬觸媒粒子之產氫速率2500(ml/g.min)相比較,產氫活性相當,如第3圖所示。但若考量價格因素,則本發明之鈷支撐於鐵上之奈米粒子觸媒因含鐵,故其價格較習用之 純鈷觸媒便宜。 The hydrogen production activity test method is as follows: a 5 wt% sodium borohydride (NaBH 4 ) solution and a weight percent concentration of 5 wt% sodium hydroxide (NaOH) solution are prepared in deionized water, and a hydrogen production device is set up to set a constant temperature. The bath temperature was 298 K at room temperature. Weigh a suitable amount of about 10 mg of catalyst into a round bottom single-necked flask, then inject 5 wt% sodium borohydride (NaBH 4 ) solution and 10 wt% sodium hydroxide (NaOH) solution into 10 ml, at which time a large number of bubbles generate this bubble. That is, hydrogen gas, the amount of production can be recorded on the graduated scale. It is found that the average hydrogen production rate of the iron-cobalt core-shell catalyst nanoparticles is 2200 (ml/g.min), and if compared with the hydrogen production rate of cobalt metal catalyst particles of 2500 (ml/g.min), The hydrogen production activity is comparable, as shown in Figure 3. However, if the price factor is considered, the nanoparticle catalyst supported on the iron of the cobalt of the present invention is cheaper than the conventional pure cobalt catalyst because it contains iron.

上述之實施例僅為例示性說明本發明之特點及其功效,而非用於限制本發明之實質技術內容的範圍。任何熟悉此技藝之人士均可在不違背本發明之精神及範疇下,對上述實施例進行修飾與變化。因此,本發明之權利保護範圍,應如後述之申請專利範圍所列。 The above-described embodiments are merely illustrative of the features and functions of the present invention, and are not intended to limit the scope of the technical scope of the present invention. Modifications and variations of the above-described embodiments can be made by those skilled in the art without departing from the spirit and scope of the invention. Therefore, the scope of protection of the present invention should be as set forth in the scope of the claims described below.

S101~S104‧‧‧為鈷複合觸媒之製程步驟 S101~S104‧‧‧ is the process of cobalt composite catalyst

第1圖係為本發明鈷複合觸媒製備流程示意圖。 Fig. 1 is a schematic view showing the preparation process of the cobalt composite catalyst of the present invention.

第2圖係為本發明實施例一之鈷複合觸媒產氫前後X-ray繞射圖譜。 Fig. 2 is a X-ray diffraction pattern before and after hydrogen production of the cobalt composite catalyst of the first embodiment of the present invention.

第3圖係為本發明實施例一之鈷複合觸媒與鈷金屬粒子產氫速率活性比較圖。 Fig. 3 is a graph comparing the hydrogen production rate activity of the cobalt composite catalyst and the cobalt metal particles according to the first embodiment of the present invention.

S101~S104‧‧‧為鈷複合觸媒之製程步驟 S101~S104‧‧‧ is the process of cobalt composite catalyst

Claims (7)

一種鈷複合觸媒製備方法,其步驟包括:(A)提供一含鐵化合物及一含鈷化合物分別溶於水中,形成一含鐵溶液及一含鈷溶液;(B)將該含鐵溶液加入一硼氫化鈉溶液;(C)將該含鈷溶液加入該含鐵溶液,得一鐵鈷混合溶液;(D)提供該硼氫化鈉溶液加入該鐵鈷混合溶液而形成金屬鈷支撐於奈米金屬鐵粒子上之複合觸媒;藉此,控制該含鈷溶液、該含鐵溶液及該硼氫化鈉溶液之濃度組合,達到以該金屬鈷為活性中心,並利用該奈米金屬鐵作為載體提高該金屬鈷粒子之活性面積進行產氫反應。 A method for preparing a cobalt composite catalyst, comprising the steps of: (A) providing an iron-containing compound and a cobalt-containing compound dissolved in water to form an iron-containing solution and a cobalt-containing solution; (B) adding the iron-containing solution a sodium borohydride solution; (C) adding the cobalt-containing solution to the iron-containing solution to obtain a mixed solution of iron and cobalt; (D) providing the sodium borohydride solution to the iron-cobalt mixed solution to form a metal cobalt support in the nanometer a composite catalyst on the metal iron particles; thereby controlling a concentration combination of the cobalt-containing solution, the iron-containing solution, and the sodium borohydride solution to achieve the active center of the metal cobalt, and using the nano-metal iron as a carrier The active area of the metal cobalt particles is increased to carry out a hydrogen production reaction. 如申請專利範圍第1項一種鈷複合觸媒製備方法,其中,含鐵化合物係為氯化鐵、硝酸鐵、醋酸鐵鹽或其組合之群組之一。 A method for preparing a cobalt composite catalyst according to the first aspect of the invention, wherein the iron-containing compound is one of a group of ferric chloride, iron nitrate, iron acetate or a combination thereof. 如申請專利範圍第1項一種鈷複合觸媒製備方法,其中,含鈷化合物係為氯化鈷、硝酸鈷、醋酸鈷鹽或其組合之群組之一。 A method for preparing a cobalt composite catalyst according to the first aspect of the invention, wherein the cobalt-containing compound is one of the group of cobalt chloride, cobalt nitrate, cobalt acetate or a combination thereof. 如申請專利範圍第1項一種鈷複合觸媒製備方法,其中,還原劑濃度為1wt%至10wt%。 A method for preparing a cobalt composite catalyst according to the first aspect of the invention, wherein the reducing agent concentration is from 1% by weight to 10% by weight. 如申請專利範圍第1項一種鈷複合觸媒製備方法,其中,含鈷化合物濃度為0.01M至0.05M。 A method for preparing a cobalt composite catalyst according to the first aspect of the patent application, wherein the cobalt-containing compound has a concentration of 0.01 M to 0.05 M. 如申請專利範圍第1項一種鈷複合觸媒製備方法,其中,含鐵化合物濃度為0.01M至0.05M。 A method for preparing a cobalt composite catalyst according to the first aspect of the patent application, wherein the concentration of the iron-containing compound is from 0.01 M to 0.05 M. 如申請專利範圍第1項一種鈷複合觸媒製備方法,其中,為了取出鈷複合觸媒更進一步提出另外三個步驟:步驟(E)係為利用磁性吸附觸媒粉末;步驟(F)利用過濾法過濾出該鈷複合觸媒;步驟(G)將該鈷複合觸媒烘乾及研磨。 For example, in the preparation method of the cobalt composite catalyst according to the first aspect of the patent application, in order to take out the cobalt composite catalyst, another three steps are further proposed: the step (E) is to utilize the magnetic adsorption catalyst powder; the step (F) is to use the filtration. The cobalt composite catalyst is filtered out; and the cobalt composite catalyst is dried and ground in step (G).
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WO2011073120A1 (en) * 2009-12-17 2011-06-23 Basf Se Metal oxide support material containing nanoscaled iron-platinum group metal particles

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2011073120A1 (en) * 2009-12-17 2011-06-23 Basf Se Metal oxide support material containing nanoscaled iron-platinum group metal particles

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