TW201623140A - Hydrogen storage composite and method for manufacturing the same - Google Patents

Hydrogen storage composite and method for manufacturing the same Download PDF

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TW201623140A
TW201623140A TW103144440A TW103144440A TW201623140A TW 201623140 A TW201623140 A TW 201623140A TW 103144440 A TW103144440 A TW 103144440A TW 103144440 A TW103144440 A TW 103144440A TW 201623140 A TW201623140 A TW 201623140A
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hydrogen storage
catalyst
carbon
storage composite
hydrogen
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TWI534076B (en
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黃軍儒
曾宦雄
黃蒨芸
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財團法人工業技術研究院
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Abstract

Disclosed is a hydrogen storage composite, including a hydrogen storage material, a carbon support embedded on a surface of the hydrogen storage material, and a catalyst covering the carbon support, wherein the carbon support has at least one dimension of 10 nm to 100 nm.

Description

儲氫複材與其形成方法 Hydrogen storage composite material and forming method thereof

本發明係關於儲氫複材,更特別關於其採用的觸媒態樣。 The present invention relates to hydrogen storage composites, and more particularly to the catalytic properties employed therein.

氫能為潔淨的能源選擇,其關鍵技術之一就是安全且低成本地儲存與輸送氫氣。由於鋼瓶高壓氫氣儲運以及液態氫儲運的方式存在著儲氫密度低、安全性差、耗能、及成本高的問題,因此最具潛力的儲氫方式乃是以金屬或合金材料儲存氫。儲氫合金的原理是利用外界環境的溫度、及/或壓力改變,使合金吸收氫氣而形成合金氫化物。當需要利用氫氣時,再由合金氫化物釋放氫氣。儲放氫氣的過程如擴散、相變、及化合等階段,均受到熱效應與速度的限制而不易爆炸。 Hydrogen is a clean energy source and one of its key technologies is the safe and low cost storage and delivery of hydrogen. Because of the low hydrogen storage density, poor safety, energy consumption, and high cost of high-pressure hydrogen storage and transportation of cylinders, the most potential hydrogen storage method is to store hydrogen by metal or alloy materials. The principle of the hydrogen storage alloy is to use the temperature and/or pressure changes of the external environment to cause the alloy to absorb hydrogen to form an alloy hydride. When hydrogen is required to be used, hydrogen is released from the alloy hydride. The process of storing and releasing hydrogen, such as diffusion, phase change, and chemical combination, is limited by thermal effects and speed and is not explosive.

利用金屬氫化物作為儲氫媒介的優點為貯氫密度高、安全程度高、以及氫氣釋放純度高。然而目前儲氫合金的缺點在於高儲氫量的合金如鎂基合金,其吸放氫動力差,放氫操作溫度仍過高(鎂基合金一般需要300℃以上才能放氫),大幅降低其實用性。綜上所述,目前亟需可在較低的溫度下吸放氫的儲氫複材,以利未來氫能源之運用。 The advantages of using metal hydride as a hydrogen storage medium are high hydrogen storage density, high safety, and high hydrogen release purity. However, the current disadvantage of hydrogen storage alloys is that alloys with high hydrogen storage capacity, such as magnesium-based alloys, have poor hydrogen absorption and desorption power, and the hydrogen discharge operation temperature is still too high (magnesium-based alloys generally require more than 300 °C to release hydrogen), which greatly reduces their Practicality. In summary, there is an urgent need for a hydrogen storage composite that can absorb and release hydrogen at a lower temperature to facilitate the future use of hydrogen energy.

本發明一實施例提供之儲氫複材,包括:儲氫材料; 碳材載體,鑲嵌至儲氫材料之表面;以及觸媒,披覆於碳材載體之表面上,其中碳材載體之至少一維的尺寸介於10nm至100nm之間。 A hydrogen storage composite material according to an embodiment of the invention includes: a hydrogen storage material; a carbon material carrier embedded in the surface of the hydrogen storage material; and a catalyst coated on the surface of the carbon material carrier, wherein at least one dimension of the carbon material carrier is between 10 nm and 100 nm.

本發明一實施例提供之儲氫複材的形成方法,包 括:將觸媒披覆於碳材載體之表面;以及將表面披覆有觸媒之碳材載體鑲嵌至儲氫材料之表面,以形成儲氫複材,其中碳材載體之至少一維的尺寸介於10nm至100nm之間。 A method for forming a hydrogen storage composite material according to an embodiment of the present invention, comprising The method comprises: coating a catalyst on a surface of the carbon material carrier; and embedding a carbon material carrier coated with a catalyst on the surface of the hydrogen storage material to form a hydrogen storage composite material, wherein the carbon material carrier is at least one-dimensional The size is between 10 nm and 100 nm.

10‧‧‧儲氫複材 10‧‧‧ Hydrogen storage composite

11‧‧‧觸媒 11‧‧‧ Catalyst

13‧‧‧碳材載體 13‧‧‧Carbon carrier

15‧‧‧儲氫材料 15‧‧‧ Hydrogen storage materials

第1圖係本發明一實施例中,儲氫複材的示意圖。 Fig. 1 is a schematic view showing a hydrogen storage composite material in an embodiment of the present invention.

本發明一實施例提供儲氫複材的形成方法,主要包括兩步驟:(1)將觸媒11披覆於碳材載體13之表面;以及(2)將表面披覆有觸媒11之碳材載體13鑲嵌至儲氫材料15之表面,以形成儲氫複材10,如第1圖所示。為了增進觸媒催化放氫的效果,本發明將觸媒11披覆在碳材載體13上,使觸媒11得以維持奈米尺寸且具備良好的分散性。上述觸媒11披覆於碳材載體13的方法可為熱裂解法,比如在手套箱中精秤觸媒前驅物與碳材載體13後,將其置於球磨罐內並放置球磨珠進行球磨混合。在本發明一實施例中,此球磨製程歷時15至30分鐘。上述球磨除了使觸媒前驅物與碳材載體13均勻混合外,同時將觸媒前驅物嵌入於碳材載體13表面。取適量之球磨混合後的複合材料進行DSC分析,以確認複合材料之熱裂解溫度範圍,作為管型加熱爐末溫持溫之依據。接著將球 磨混合好之複合材料置於加熱爐中,抽真空並進行氬氣之反覆淨化(purge)後,於氬氣氣氛下加熱至複合材料的熱裂解溫度並持溫一段時間,即可還原觸媒前驅物以披覆觸媒11於碳材載體13的表面上。在本發明一實施例中,上述熱裂解歷時0.5至3小時。熱裂解法的特點是其觸媒分散性佳,處理時間短,可快速結合觸媒11與碳材載體13。由於熱裂解法快速升降溫的優勢,不會因加熱時間過長而破壞觸媒11與碳材載體13。經適度地調觸媒11比例,可控制觸媒11穩定接合於碳材載體13的表面上,藉碳材載體13之溢出作用(spillover)提升觸媒放氫效率。 An embodiment of the present invention provides a method for forming a hydrogen storage composite material, which mainly comprises two steps: (1) coating the catalyst 11 on the surface of the carbon material carrier 13; and (2) coating the surface with the carbon of the catalyst 11 The material carrier 13 is inlaid to the surface of the hydrogen storage material 15 to form a hydrogen storage composite 10 as shown in FIG. In order to enhance the effect of catalyst catalytic hydrogen evolution, the present invention coats the catalyst 11 on the carbon material carrier 13 to maintain the nanoparticle size of the catalyst 11 and to have good dispersibility. The method for coating the above-mentioned catalyst 11 on the carbon material carrier 13 may be a thermal cracking method, such as after weighing the catalyst precursor and the carbon material carrier 13 in a glove box, placing it in a ball grinding tank and placing the ball grinding beads for ball milling. mixing. In an embodiment of the invention, the ball milling process lasts from 15 to 30 minutes. The ball milling described above, in addition to uniformly mixing the catalyst precursor with the carbon material carrier 13, simultaneously embeds the catalyst precursor on the surface of the carbon material carrier 13. The appropriate amount of the ball milled composite material was subjected to DSC analysis to confirm the thermal cracking temperature range of the composite material, which was used as the basis for the temperature maintenance of the tubular heating furnace. Then the ball The mixed and mixed composite material is placed in a heating furnace, vacuumed and subjected to urethane purge, and then heated to an argon atmosphere to a thermal cracking temperature of the composite material and held for a period of time to restore the catalyst. The precursor coats the catalyst 11 on the surface of the carbon material carrier 13. In an embodiment of the invention, the thermal cracking described above lasts from 0.5 to 3 hours. The thermal cracking method is characterized in that the catalyst has good dispersibility and short processing time, and the catalyst 11 and the carbon carrier 13 can be quickly combined. Due to the advantage of rapid thermal expansion of the thermal cracking method, the catalyst 11 and the carbon carrier 13 are not destroyed by the excessive heating time. By appropriately adjusting the ratio of the catalyst 11, the catalyst 11 can be controlled to be stably bonded to the surface of the carbon material carrier 13, and the hydrogen absorption efficiency of the catalyst can be improved by the spillover of the carbon material carrier 13.

在本發明一實施例中,觸媒11與碳材載體13之重量 比介於20:80至50:50之間。若觸媒11之比例過高,則觸媒11不易均勻披覆於碳材載體13表面而形成團聚、粗化。若觸媒11之比例過低,則催化活性較差。在本發明一實施例中,碳材載體13包括奈米碳管、石墨、石墨烯、活性碳、或上述之組合,且碳材載體13之至少一維的尺寸介於10nm至100nm之間。若碳材載體13的所有維度尺寸過大,則披覆觸媒11之尺寸可能會過大而降低其放氫性能。以奈米碳管為例,其長度可介於20nm-100nm之間,且管徑可介於3nm-8nm之間。在本發明一實施例中,觸媒11包括Ni、Fe、Co、V、Ti、Pt、Pd、Cu、Cr、或Ag。 In an embodiment of the invention, the weight of the catalyst 11 and the carbon material carrier 13 The ratio is between 20:80 and 50:50. When the ratio of the catalyst 11 is too high, the catalyst 11 is less likely to be uniformly coated on the surface of the carbon material carrier 13 to form agglomeration and coarsening. If the ratio of the catalyst 11 is too low, the catalytic activity is poor. In an embodiment of the invention, the carbon material carrier 13 comprises a carbon nanotube, graphite, graphene, activated carbon, or a combination thereof, and at least one dimension of the carbon material carrier 13 is between 10 nm and 100 nm. If all the dimensional dimensions of the carbon material carrier 13 are too large, the size of the coating catalyst 11 may be excessively large to lower its hydrogen releasing performance. Taking a carbon nanotube as an example, the length may be between 20 nm and 100 nm, and the diameter may be between 3 nm and 8 nm. In an embodiment of the invention, the catalyst 11 comprises Ni, Fe, Co, V, Ti, Pt, Pd, Cu, Cr, or Ag.

將表面披覆有觸媒11之碳材載體13鑲嵌至儲氫材料 15之表面,以形成儲氫複材10之步驟可為球磨法。舉例來說,可將表面披覆有觸媒11之碳材載體13與儲氫材料15置於球磨罐中,於氬氣下進行球磨製程以形成儲氫複材10。球磨珠可為碳化鎢或不鏽鋼,其直徑介於1mm至5mm之間。若球磨珠之直徑過小,則 研磨能量較低而機械嵌合的效率較差。若球磨珠之直徑過大,則容易在研磨珠與研磨罐之間的空隙產生死角,而使部分粉體無法充分被磨珠撞擊而嵌合。球磨珠與待磨物(表面披覆有觸媒11之碳材載體13及儲氫材料15)之重量比介於10:1至50:1之間。若待磨物之比例過高,則研磨、嵌合的效率較差。若待磨物之比例過低,則容易造成研磨珠的磨耗。球磨方式可為行星式旋轉、攪拌、或振盪,且球磨製程歷時15分鐘至30分鐘。若球磨製程歷時過短,則機械嵌合的效果較差。若球磨製程歷時過長,則可能造成觸媒11從碳材載體13表面脫落,並與儲氫材料15產生合金化。利用機械力研磨的撞擊方式,可將表面披覆有觸媒11之碳材載體13直接鑲嵌於儲氫材料15的表面上,且不與該儲氫材料形成合金,使觸媒11可以發揮催化活性,讓儲氫材料15在較低的溫度下有效地進行放氫。由於已先行將觸媒11披覆於碳材載體13表面,除了有助於均勻分散觸媒11外,更可形成保護界面,降低觸媒11在高能球磨中與儲氫材料15合金化的可能性。 The carbon material carrier 13 coated with the catalyst 11 is inlaid to the hydrogen storage material The step of forming the hydrogen storage composite 10 may be a ball milling method. For example, the carbon material carrier 13 and the hydrogen storage material 15 coated with the catalyst 11 may be placed in a ball mill tank, and subjected to a ball milling process under argon to form a hydrogen storage composite material 10. The ball beads can be tungsten carbide or stainless steel and have a diameter between 1 mm and 5 mm. If the diameter of the ball is too small, then The grinding energy is lower and the mechanical fitting is less efficient. If the diameter of the ball bead is too large, it is easy to cause a dead space in the gap between the grinding bead and the grinding can, and some of the powder cannot be sufficiently impacted by the bead to be fitted. The weight ratio of the ball beads to the object to be abraded (the carbon material carrier 13 and the hydrogen storage material 15 having the catalyst 11 coated on the surface) is between 10:1 and 50:1. If the proportion of the material to be grounded is too high, the efficiency of grinding and fitting is poor. If the proportion of the material to be grounded is too low, the grinding beads are easily worn. The ball milling method can be planetary rotation, stirring, or oscillation, and the ball milling process lasts from 15 minutes to 30 minutes. If the ball milling process is too short, the mechanical fitting effect is poor. If the ball milling process takes too long, the catalyst 11 may be peeled off from the surface of the carbon material carrier 13 and alloyed with the hydrogen storage material 15. The carbon material carrier 13 having the catalyst 11 coated on the surface thereof is directly embedded on the surface of the hydrogen storage material 15 by an impact method of mechanical force grinding, and does not form an alloy with the hydrogen storage material, so that the catalyst 11 can be catalyzed. The activity allows the hydrogen storage material 15 to efficiently perform hydrogen evolution at a lower temperature. Since the catalyst 11 is first coated on the surface of the carbon material carrier 13, in addition to helping to uniformly disperse the catalyst 11, a protective interface can be formed to reduce the possibility of alloying of the catalyst 11 with the hydrogen storage material 15 in the high energy ball milling. Sex.

經上述球磨製程後,表面披覆有觸媒11之碳材載體 13將會分布在儲氫材料15的表面或者材料本身晶粒之間的界面(晶界)上。儲氫材料15中的氫原子經過碳材載體13的表面時,將產生溢出作用,即氫原子於兩相的交界處直接進行催化反應,而有助於降低放氫的活化能能障,進而提升儲氫複材10的放氫反應速率。 After the above ball milling process, the surface is covered with a carbon material carrier of the catalyst 11 13 will be distributed on the surface of the hydrogen storage material 15 or the interface (grain boundary) between the grains of the material itself. When the hydrogen atoms in the hydrogen storage material 15 pass through the surface of the carbon material carrier 13, an overflow action occurs, that is, hydrogen atoms directly undergo catalytic reaction at the boundary of the two phases, thereby contributing to a reduction in the activation energy barrier of hydrogen release, and further The rate of hydrogen evolution reaction of the hydrogen storage composite 10 is increased.

在本發明一實施例中,儲氫材料15可為鎂、氫化鎂、 或鎂基合金。在本發明一實施例中,碳材載體13與觸媒11之總重占儲氫複料之1wt%至5wt%之間。若碳材載體13與觸媒11之比例過 高,則會佔據儲氫複材10太多的重量而損失一些儲氫量。若碳材載體13與觸媒11之比例過低,則儲氫複材10之儲放氫反應的催化活性不足。 In an embodiment of the invention, the hydrogen storage material 15 may be magnesium, magnesium hydride, Or magnesium based alloy. In an embodiment of the invention, the total weight of the carbon material carrier 13 and the catalyst 11 is between 1% and 5% by weight of the hydrogen storage material. If the ratio of the carbon material carrier 13 to the catalyst 11 has passed If it is high, it will occupy too much weight of the hydrogen storage composite material 10 and lose some hydrogen storage capacity. If the ratio of the carbon material carrier 13 to the catalyst 11 is too low, the catalytic activity of the hydrogen storage reaction of the hydrogen storage composite material 10 is insufficient.

在本發明一實施例中,儲氫材料15之尺寸約介於100nm~1mm之間。若儲氫材料15之尺寸過大,則因粒徑大導致儲氫性能降低。若儲氫材料15之尺寸過小,則碳材載體13不易披覆。 In an embodiment of the invention, the hydrogen storage material 15 has a size between about 100 nm and 1 mm. If the size of the hydrogen storage material 15 is too large, the hydrogen storage performance is lowered due to the large particle size. If the size of the hydrogen storage material 15 is too small, the carbon material carrier 13 is not easily coated.

為了讓本發明之上述和其他目的、特徵、和優點能更明顯易懂,下文特舉數實施例配合所附圖示,作詳細說明如下: The above and other objects, features, and advantages of the present invention will become more apparent and understood.

實施例 Example 實施例1-1 Example 1-1

取0.2g之碳酸鎳(Alfa Aesar,Nickell(II)acetate tetrahydrate,98+%)、0.8g之奈米碳管(購自ALDRICH之單壁奈米碳管,管長約30nm,且管徑約5nm)、及20g之碳化鎢磨球置入球磨罐中,再將球磨罐置入震盪球磨機(SPEX CertiPrep®,Inc.,8000M)中球磨15分鐘,使碳酸鎳嵌入奈米碳管表面。接著取少量球磨後的樣品進行DSC測試,得知樣品之熱裂解溫度為約400℃。接著將球磨混合好的樣品置於加熱爐中,抽真空並進行氬氣之反覆淨化(purge)後,在氬氣氣氛下將其由室溫加熱至400℃並持溫1小時。使碳酸鎳熱裂解並還原為鎳披覆於奈米碳管表面。 Take 0.2g of nickel carbonate (Alfa Aesar, Nickell (II) acetate tetrahydrate, 98+%), 0.8g of carbon nanotubes (single-walled carbon nanotubes purchased from ALDRICH, the tube length is about 30nm, and the diameter is about 5nm And 20 g of tungsten carbide grinding balls were placed in a ball mill jar, and the ball mill jar was placed in an oscillating ball mill (SPEX CertiPrep®, Inc., 8000 M) for 15 minutes to embed nickel carbonate on the surface of the carbon nanotubes. A small amount of the ball milled sample was then subjected to DSC testing to find that the sample had a thermal cracking temperature of about 400 °C. Next, the ball-milled sample was placed in a heating furnace, evacuated and subjected to argon purge, and then heated from room temperature to 400 ° C under an argon atmosphere for 1 hour. The nickel carbonate is thermally cracked and reduced to nickel over the surface of the carbon nanotube.

接著取1重量份之上述鎳披覆於奈米碳管表面的複合觸媒、99重量份之鎂粉、以及2000重量份之碳化鎢磨球置入球磨罐中,再將球磨罐置入震盪球磨機(SPEX CertiPrep®,Inc.,8000M)中球磨15分鐘,使複合觸媒嵌入鎂粉中以完成儲氫複材。 Then, 1 part by weight of the above composite catalyst coated with nickel on the surface of the carbon nanotube, 99 parts by weight of magnesium powder, and 2000 parts by weight of tungsten carbide grinding balls are placed in a ball mill tank, and then the ball mill jar is placed in a shock chamber. The ball mill (SPEX CertiPrep®, Inc., 8000M) was ball milled for 15 minutes to embed the composite catalyst into the magnesium powder to complete the hydrogen storage composite.

比較例1 Comparative example 1

取1重量份之奈米碳管、99重量份之鎂粉、以及2000重量份之碳化鎢磨球置入球磨罐中,再將球磨罐置入震盪球磨機(SPEX CertiPrep®,Inc.,8000M)中球磨15分鐘,使奈米碳管嵌入鎂粉中以完成儲氫複材。此比較例之奈米碳管表面上未披覆有任何觸媒。 1 part by weight of carbon nanotubes, 99 parts by weight of magnesium powder, and 2000 parts by weight of tungsten carbide grinding balls were placed in a ball mill jar, and then the ball mill jar was placed in an oscillating ball mill (SPEX CertiPrep®, Inc., 8000M). The ball was milled for 15 minutes, and the carbon nanotubes were embedded in the magnesium powder to complete the hydrogen storage composite. The surface of the carbon nanotube of this comparative example was not coated with any catalyst.

比較例2 Comparative example 2

取100重量份之鎂粉以及2000重量份之碳化鎢磨球置入球磨罐中,再將球磨罐置入震盪球磨機(SPEX CertiPrep®,Inc.,8000M)中球磨2小時,以完成球磨後之鎂粉。 100 parts by weight of magnesium powder and 2000 parts by weight of tungsten carbide grinding balls were placed in a ball mill jar, and then the ball mill was placed in an oscillating ball mill (SPEX CertiPrep®, Inc., 8000 M) for 2 hours to complete the ball milling. Magnesium powder.

比較例3 Comparative example 3

首先將α-Al2O3粉體進行敏化處理(Sensitization Processing)。敏化劑的調配是取5g的SnCl2溶解於7.5mL之37%的HCl(1)中,再將整體溶液以去離子水稀釋至50mL後即可使用。而後將2g之α-Al2O3粉體(購自大明株式會社之TM-DAR,尺寸介於100nm至1mm之間)浸入上述調配好的敏化劑中,於室溫下攪拌5分鐘,使Sn2+離子吸附在α-Al2O3粉體表面上,再利用離心方式去除濾液以得敏化之α-Al2O3粉體。將敏化後的α-Al2O3粉體浸入45mL的氯化鈀水溶液中,該溶液的調配乃是取1g的PdCl2溶解於30mL之37%的HCl(1)中,再將整體溶液以去離子水稀釋至100mL後即可使用。這時粉體表面上的Sn2+離子會將鈀離子還原而吸附在α-Al2O3粉體表面,待反應5分鐘的時間後,將粉體以離心方式收集,則得到複合觸媒α-Al2O3/Pd。 First, the α-Al 2 O 3 powder was subjected to sensitization processing. The sensitizer was prepared by dissolving 5 g of SnCl 2 in 7.5 mL of 37% HCl (1) , and then diluting the whole solution to 50 mL with deionized water. Then, 2 g of α-Al 2 O 3 powder (TM-DAR from Daming Co., Ltd., having a size between 100 nm and 1 mm) was immersed in the above-mentioned formulated sensitizer, and stirred at room temperature for 5 minutes. The Sn 2+ ion is adsorbed on the surface of the α-Al 2 O 3 powder, and the filtrate is removed by centrifugation to obtain a sensitized α-Al 2 O 3 powder. The sensitized α-Al 2 O 3 powder was immersed in a 45 mL aqueous solution of palladium chloride. The solution was prepared by dissolving 1 g of PdCl 2 in 30 mL of 37% HCl (1) , and then the whole solution. It can be used after diluting to 100 mL with deionized water. At this time, the Sn 2+ ions on the surface of the powder will reduce the palladium ions and adsorb on the surface of the α-Al 2 O 3 powder. After the reaction for 5 minutes, the powder is collected by centrifugation to obtain the composite catalyst α. -Al 2 O 3 /Pd.

將上述複合觸媒α-Al2O3/Pd以機械力的方式,將其鑲嵌於氫化鎂的儲氫材料上。首先將氫化鎂與複合觸媒α-Al2O3/Pd以重量百分比92:8的比例混合後,再將混合後的粉體與碳化鎢磨 球以重量比1:32的方式填入碳化鎢研磨罐體中,並充填氬氣。將研磨罐置入震盪球磨機(SPEX CertiPrep®,Inc.,8000M)中以30分鐘的時間進行球磨撞擊,進而將複合觸媒α-Al2O3/Pd鑲嵌於氫化鎂的表面上,形成儲氫複材。 The above composite catalyst α-Al 2 O 3 /Pd is mechanically embedded in a hydrogen storage material of magnesium hydride. First, the magnesium hydride and the composite catalyst α-Al 2 O 3 /Pd are mixed in a ratio of 92:8 by weight, and then the mixed powder and the tungsten carbide grinding ball are filled into the carbonization at a weight ratio of 1:32. Tungsten is ground in the tank and filled with argon. The grinding jar was placed in an oscillating ball mill (SPEX CertiPrep®, Inc., 8000M) for 30 minutes to perform ball milling impact, and then the composite catalyst α-Al 2 O 3 /Pd was embedded on the surface of the magnesium hydride to form a reservoir. Hydrogen composite material.

接著採用Sievert系統確認實施例1-1與比較例1至4之產物的儲放氫量。在密閉且固定的容積內放入上述產物,藉由量測充放氫過程中氣體壓力的變化量來推知儲放氫量。吸氫測試所採用的氫氣壓力為20atm,且溫度為300℃。放氫測試所採用的氫氣壓力低於1atm。放氫的量測是讓材料於第一次吸氫後,使材料於<1atm的壓力環境下充分放氫一天,而後量測其第二次吸氫曲線來判斷該材料的放氫量。上述量測結果如第1表所示: The amount of hydrogen storage and desorption of the products of Example 1-1 and Comparative Examples 1 to 4 was confirmed by the Sievert system. The above product is placed in a sealed and fixed volume, and the amount of hydrogen stored and discharged is measured by measuring the amount of change in gas pressure during charge and discharge. The hydrogen pressure test used a hydrogen pressure of 20 atm and a temperature of 300 °C. The hydrogen pressure used in the hydrogen evolution test was less than 1 atm. The measurement of hydrogen release is to let the material fully hydrogen release under the pressure environment of <1 atm for one day after the first hydrogen absorption, and then measure the second hydrogen absorption curve to determine the hydrogen release amount of the material. The above measurement results are shown in Table 1:

由第1表可知,奈米碳管上未批覆觸媒的儲氫複材(比較例1),其放氫量遠低於奈米碳管上批覆觸媒的儲氫複材(實施例1-1)。另一方面,若將奈米碳管置換為氧化鋁(比較例3),其吸氫量與放氫量均低於奈米碳管作為載體之複合觸媒(實施例1-1)。至於鎂粉(比較例2)之吸氫量則低於表面鑲嵌有複合觸媒的儲氫複材(實施例1-1)。 It can be seen from the first table that the hydrogen storage composite material (Comparative Example 1) on which the catalyst is not coated on the carbon nanotubes has a hydrogen release amount much lower than that of the hydrogen storage composite material of the catalyst on the carbon nanotubes (Example 1). -1). On the other hand, when the carbon nanotubes were replaced with alumina (Comparative Example 3), both the amount of hydrogen absorption and the amount of hydrogen released were lower than those of the composite catalyst of the carbon nanotubes as a carrier (Example 1-1). As for the magnesium powder (Comparative Example 2), the amount of hydrogen absorption was lower than that of the hydrogen storage composite in which the composite catalyst was embedded (Example 1-1).

實施例1-2 Example 1-2

與實施例1-1類似,差別在於複合觸媒與鎂粉的重量比為 3:97。其他將鎳披覆於奈米碳管表面的熱裂解法、將複合觸媒嵌入鎂粉的球磨製程參數均與實施例1-1類似。 Similar to Example 1-1, the difference is that the weight ratio of the composite catalyst to the magnesium powder is 3:97. Other thermal cracking methods in which nickel was coated on the surface of the carbon nanotubes, and ball milling process parameters in which the composite catalyst was embedded in the magnesium powder were similar to those in Example 1-1.

實施例1-3 Examples 1-3

與實施例1-1類似,差別在於複合觸媒與鎂粉的重量比為5:95。其他將鎳披覆於奈米碳管表面的熱裂解法、將複合觸媒嵌入鎂粉的球磨製程參數均與實施例1-1類似。 Similar to Example 1-1, the difference was that the weight ratio of the composite catalyst to the magnesium powder was 5:95. Other thermal cracking methods in which nickel was coated on the surface of the carbon nanotubes, and ball milling process parameters in which the composite catalyst was embedded in the magnesium powder were similar to those in Example 1-1.

接著採用Sievert系統確認實施例1-1至1-3與比較例1之產物的儲放氫量。在密閉且固定的容積內放入上述產物,藉由量測充放氫過程中氣體壓力的變化量來推知儲放氫量。吸氫測試所採用的氫氣壓力為20atm,且溫度為300℃或150℃。放氫測試所採用的氫氣壓力低於1atm。放氫的量測是讓材料於第一次吸氫後,使材料於<1atm的壓力環境下充分放氫一天,而後量測其第二次吸氫曲線來判斷該材料的放氫量。上述量測結果如第2表所示: The amount of hydrogen storage and desorption of the products of Examples 1-1 to 1-3 and Comparative Example 1 was then confirmed using a Sievert system. The above product is placed in a sealed and fixed volume, and the amount of hydrogen stored and discharged is measured by measuring the amount of change in gas pressure during charge and discharge. The hydrogen pressure test used a hydrogen pressure of 20 atm and a temperature of 300 ° C or 150 ° C. The hydrogen pressure used in the hydrogen evolution test was less than 1 atm. The measurement of hydrogen release is to let the material fully hydrogen release under the pressure environment of <1 atm for one day after the first hydrogen absorption, and then measure the second hydrogen absorption curve to determine the hydrogen release amount of the material. The above measurement results are shown in Table 2:

由第2表可知,奈米碳管上未批覆觸媒的儲氫複材(比較例1),其放氫量遠低於奈米碳管上批覆觸媒的儲氫複材(實施例1-1至1-3)。 It can be seen from the second table that the hydrogen storage composite material (Comparative Example 1) on which the catalyst is not coated on the carbon nanotubes has a hydrogen release amount much lower than that of the hydrogen storage composite material of the catalyst on the carbon nanotubes (Example 1). -1 to 1-3).

10‧‧‧儲氫複材 10‧‧‧ Hydrogen storage composite

11‧‧‧觸媒 11‧‧‧ Catalyst

13‧‧‧碳材載體 13‧‧‧Carbon carrier

15‧‧‧儲氫材料 15‧‧‧ Hydrogen storage materials

Claims (17)

一種儲氫複材,包括:一儲氫材料;一碳材載體,鑲嵌至該儲氫材料之表面;以及一觸媒,披覆於該碳材載體之表面上,其中該碳材載體之至少一維的尺寸介於10nm至100nm之間。 A hydrogen storage composite material comprising: a hydrogen storage material; a carbon material carrier embedded in a surface of the hydrogen storage material; and a catalyst coated on a surface of the carbon material carrier, wherein the carbon material carrier is at least The one-dimensional size is between 10 nm and 100 nm. 如申請專利範圍第1項所述之儲氫複材,其中該碳材載體與該觸媒之總重占該儲氫複材之1wt%至5wt%之間。 The hydrogen storage composite according to claim 1, wherein the total weight of the carbon material carrier and the catalyst accounts for between 1% and 5% by weight of the hydrogen storage composite. 如申請專利範圍第1項所述之儲氫複材,其中該觸媒與該碳材載體之重量比介於20:80至50:50之間。 The hydrogen storage composite material according to claim 1, wherein the weight ratio of the catalyst to the carbon material carrier is between 20:80 and 50:50. 如申請專利範圍第1項所述之儲氫複材,其中該儲氫材料包括鎂、氫化鎂、或鎂基合金。 The hydrogen storage composite material according to claim 1, wherein the hydrogen storage material comprises magnesium, magnesium hydride, or a magnesium-based alloy. 如申請專利範圍第1項所述之儲氫複材,其中該碳材載體包括奈米碳管、石墨、石墨烯、活性碳、或上述之組合。 The hydrogen storage composite material according to claim 1, wherein the carbon material carrier comprises a carbon nanotube, graphite, graphene, activated carbon, or a combination thereof. 如申請專利範圍第1項所述之儲氫複材,其中該觸媒包括Ni、Fe、Co、V、Ti、Pt、Pd、Cu、Cr、或Ag。 The hydrogen storage composite material according to claim 1, wherein the catalyst comprises Ni, Fe, Co, V, Ti, Pt, Pd, Cu, Cr, or Ag. 如申請專利範圍第1項所述之儲氫複材,其中該碳材載體上所披覆的觸媒與該儲氫材料不形成合金。 The hydrogen storage composite material according to claim 1, wherein the catalyst coated on the carbon material carrier does not form an alloy with the hydrogen storage material. 一種儲氫複材的形成方法,包括:將一觸媒披覆於一碳材載體之表面;以及將表面披覆有該觸媒之該碳材載體鑲嵌至一儲氫材料之 表面,以形成一儲氫複材,其中該碳材載體之至少一維的尺寸介於10nm至100nm之間。 A method for forming a hydrogen storage composite material, comprising: coating a catalyst on a surface of a carbon material carrier; and inlaying the carbon material carrier having the catalyst surface coated with a hydrogen storage material The surface is formed to form a hydrogen storage composite, wherein at least one dimension of the carbon support is between 10 nm and 100 nm. 如申請專利範圍第8項所述之儲氫複材的形成方法,其中將該觸媒披覆於該碳材載體之表面之方法包括熱裂解法。 The method for forming a hydrogen storage composite according to claim 8, wherein the method of coating the catalyst on the surface of the carbon material carrier comprises a thermal cracking method. 如申請專利範圍第9項所述之儲氫複材的形成方法,更包括在該熱裂解法之前先以球磨法將一觸媒前驅物嵌入該碳材載體之表面。 The method for forming a hydrogen storage composite according to claim 9, further comprising first embedding a catalyst precursor on the surface of the carbon support by ball milling prior to the thermal cracking method. 如申請專利範圍第8項所述之儲氫複材的形成方法,其中將表面披覆有該觸媒之該碳材載體鑲嵌至該儲氫材料之表面的方法包括球磨法。 The method for forming a hydrogen storage composite according to claim 8, wherein the method of inlaying the carbon material carrier having the catalyst coated on the surface of the hydrogen storage material comprises a ball milling method. 如申請專利範圍第8項所述之儲氫複材的形成方法,其中該碳材載體與該觸媒之總重占該儲氫複材之1wt%至5wt%之間。 The method for forming a hydrogen storage composite according to claim 8, wherein the total weight of the carbon material carrier and the catalyst is between 1% and 5% by weight of the hydrogen storage composite. 如申請專利範圍第8項所述之儲氫複材的形成方法,其中該觸媒與該碳材載體之重量比介於20:80至50:50之間。 The method for forming a hydrogen storage composite according to claim 8, wherein the weight ratio of the catalyst to the carbon material carrier is between 20:80 and 50:50. 如申請專利範圍第8項所述之儲氫複材的形成方法,其中該儲氫材料包括鎂、氫化鎂、或鎂基合金。 The method for forming a hydrogen storage composite according to claim 8, wherein the hydrogen storage material comprises magnesium, magnesium hydride, or a magnesium-based alloy. 如申請專利範圍第8項所述之儲氫複材的形成方法,其中該碳材載體包括奈米碳管、石墨、石墨烯、活性碳、 或上述之組合。 The method for forming a hydrogen storage composite according to claim 8, wherein the carbon carrier comprises a carbon nanotube, graphite, graphene, activated carbon, Or a combination of the above. 如申請專利範圍第8項所述之儲氫複材的形成方法,其中該觸媒包括Ni、Fe、Co、V、Ti、Pt、Pd、Cu、Cr、或Ag。 The method for forming a hydrogen storage composite according to claim 8, wherein the catalyst comprises Ni, Fe, Co, V, Ti, Pt, Pd, Cu, Cr, or Ag. 如申請專利範圍第8項所述之儲氫複材的形成方法,其中該碳材載體上所披覆的觸媒與該儲氫材料不形成合金。 The method for forming a hydrogen storage composite according to claim 8, wherein the catalyst coated on the carbon material carrier does not form an alloy with the hydrogen storage material.
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TWI628290B (en) * 2017-07-05 2018-07-01 國立成功大學 Manufacturing method for rapid synthesis magnesium-based hydrogen storage materials at room temperature
TWI747148B (en) * 2019-02-01 2021-11-21 光鈺科技股份有限公司 Method for treating industrial waste acid and slag

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
TWI628290B (en) * 2017-07-05 2018-07-01 國立成功大學 Manufacturing method for rapid synthesis magnesium-based hydrogen storage materials at room temperature
TWI747148B (en) * 2019-02-01 2021-11-21 光鈺科技股份有限公司 Method for treating industrial waste acid and slag

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