TWI448421B - Porous hydrogen generating material and manufacturing method thereof - Google Patents
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- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 title claims description 128
- 239000001257 hydrogen Substances 0.000 title claims description 126
- 229910052739 hydrogen Inorganic materials 0.000 title claims description 126
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- 238000004519 manufacturing process Methods 0.000 title claims description 59
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- 239000012943 hotmelt Substances 0.000 claims description 33
- 239000010941 cobalt Substances 0.000 claims description 32
- 229910017052 cobalt Inorganic materials 0.000 claims description 32
- GUTLYIVDDKVIGB-UHFFFAOYSA-N cobalt atom Chemical compound [Co] GUTLYIVDDKVIGB-UHFFFAOYSA-N 0.000 claims description 31
- 238000000034 method Methods 0.000 claims description 25
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- 229920001059 synthetic polymer Polymers 0.000 claims description 9
- 229920003169 water-soluble polymer Polymers 0.000 claims description 9
- 229910001429 cobalt ion Inorganic materials 0.000 claims description 8
- XLJKHNWPARRRJB-UHFFFAOYSA-N cobalt(2+) Chemical group [Co+2] XLJKHNWPARRRJB-UHFFFAOYSA-N 0.000 claims description 8
- IXPNQXFRVYWDDI-UHFFFAOYSA-N 1-methyl-2,4-dioxo-1,3-diazinane-5-carboximidamide Chemical compound CN1CC(C(N)=N)C(=O)NC1=O IXPNQXFRVYWDDI-UHFFFAOYSA-N 0.000 claims description 6
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- 125000000129 anionic group Chemical group 0.000 claims description 5
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- 125000002057 carboxymethyl group Chemical group [H]OC(=O)C([H])([H])[*] 0.000 claims description 4
- GVPFVAHMJGGAJG-UHFFFAOYSA-L cobalt dichloride Chemical compound [Cl-].[Cl-].[Co+2] GVPFVAHMJGGAJG-UHFFFAOYSA-L 0.000 claims description 4
- 229920005989 resin Polymers 0.000 claims description 4
- 239000011347 resin Substances 0.000 claims description 4
- 229920002101 Chitin Polymers 0.000 claims description 3
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- NBIIXXVUZAFLBC-UHFFFAOYSA-N Phosphoric acid Chemical group OP(O)(O)=O NBIIXXVUZAFLBC-UHFFFAOYSA-N 0.000 claims description 3
- MKRNVBXERAPZOP-UHFFFAOYSA-N Starch acetate Chemical compound O1C(CO)C(OC)C(O)C(O)C1OCC1C(OC2C(C(O)C(OC)C(CO)O2)OC(C)=O)C(O)C(O)C(OC2C(OC(C)C(O)C2O)CO)O1 MKRNVBXERAPZOP-UHFFFAOYSA-N 0.000 claims description 3
- 238000000748 compression moulding Methods 0.000 claims description 3
- 229920003063 hydroxymethyl cellulose Polymers 0.000 claims description 3
- 229940031574 hydroxymethyl cellulose Drugs 0.000 claims description 3
- QAOWNCQODCNURD-UHFFFAOYSA-N sulfuric acid group Chemical group S(O)(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 claims description 3
- 239000002952 polymeric resin Substances 0.000 claims description 2
- 125000000542 sulfonic acid group Chemical group 0.000 claims description 2
- 229920003002 synthetic resin Polymers 0.000 claims description 2
- 229910010277 boron hydride Inorganic materials 0.000 claims 2
- IKCQWKJZLSDDSS-UHFFFAOYSA-N 2-formyloxyethyl formate Chemical compound O=COCCOC=O IKCQWKJZLSDDSS-UHFFFAOYSA-N 0.000 claims 1
- 229920000265 Polyparaphenylene Polymers 0.000 claims 1
- 150000001732 carboxylic acid derivatives Chemical class 0.000 claims 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 17
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- FHVDTGUDJYJELY-UHFFFAOYSA-N 6-{[2-carboxy-4,5-dihydroxy-6-(phosphanyloxy)oxan-3-yl]oxy}-4,5-dihydroxy-3-phosphanyloxane-2-carboxylic acid Chemical compound O1C(C(O)=O)C(P)C(O)C(O)C1OC1C(C(O)=O)OC(OP)C(O)C1O FHVDTGUDJYJELY-UHFFFAOYSA-N 0.000 description 13
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- HZEIHKAVLOJHDG-UHFFFAOYSA-N boranylidynecobalt Chemical compound [Co]#B HZEIHKAVLOJHDG-UHFFFAOYSA-N 0.000 description 4
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- ZOXJGFHDIHLPTG-UHFFFAOYSA-N Boron Chemical compound [B] ZOXJGFHDIHLPTG-UHFFFAOYSA-N 0.000 description 1
- 229920002134 Carboxymethyl cellulose Polymers 0.000 description 1
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Classifications
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
- Y02E60/30—Hydrogen technology
- Y02E60/36—Hydrogen production from non-carbon containing sources, e.g. by water electrolysis
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- Catalysts (AREA)
Description
本發明是有關於一種多孔性製氫材料及其製造方法,且特別是有關於一種親水性佳且製作流程簡便的多孔性製氫材料及其製造方法。 The present invention relates to a porous hydrogen producing material and a method for producing the same, and particularly relates to a porous hydrogen producing material which is excellent in hydrophilicity and simple in production flow, and a method for producing the same.
一般來說,燃料電池利用氫氣來製造電力,唯一會產生的副產品只有無污染的水和熱氣,正因如此,被許多人視為能夠取代石油的能源。再者,氫能源因其潔淨性與可儲存性讓先進國家基於能源安全與環境永續發展而積極投入。目前氫能源的利用主要是透過燃料電池裝置來使化學能變成電能,其應用涵蓋分散式發電系統、運輸載具與可攜式3C產品。然而,燃料電池距離商業化仍有一段距離,主因來自於氫氣的儲存與供應以及燃料電池的成本仍無法符合商業化的需求。 In general, fuel cells use hydrogen to make electricity. The only by-products that are produced are pollution-free water and hot gas, which is why many people see it as an energy source that can replace oil. Furthermore, hydrogen energy is actively invested in advanced countries based on energy security and environmental sustainability due to its cleanliness and storability. At present, the use of hydrogen energy is mainly through the fuel cell device to turn chemical energy into electrical energy, and its applications cover distributed power generation systems, transportation vehicles and portable 3C products. However, fuel cells are still some distance away from commercialization, mainly due to the storage and supply of hydrogen and the cost of fuel cells still not in line with commercial needs.
承上述,為了能夠供應氫氣以作用燃料電池的原料,氫氣的製造便成為非常重要的課題。目前來說,已經有許多有關製氫材料的研究以及開發,其中有很多製氫材料會使用水作為氫氣的製造來源。一般來說,製氫材料包括載體、製氫劑以及觸媒,將水加入製氫材料後,觸媒會進行催化以產生氫氣。然而,現有的載體通常是選自粉體結構,而粉體結構緻密會造成製氫材料的滲水性不佳,且使得產氫效率下降。另外,一般的粉體結構會在產氫的過程中容 易崩解,而使得載體中的觸媒不易回收再利用,造成製造的成本增加。 In view of the above, in order to supply hydrogen gas to act as a raw material for a fuel cell, the production of hydrogen has become a very important issue. At present, there are many researches and developments on hydrogen production materials, many of which use water as a source of hydrogen production. Generally, hydrogen-generating materials include a carrier, a hydrogen-generating agent, and a catalyst. After water is added to the hydrogen-generating material, the catalyst is catalyzed to generate hydrogen. However, the conventional carrier is usually selected from a powder structure, and the compact structure of the powder causes poor water permeability of the hydrogen producing material and causes a decrease in hydrogen production efficiency. In addition, the general powder structure will be in the process of hydrogen production. It is easy to disintegrate, and the catalyst in the carrier is not easily recycled and reused, resulting in an increase in manufacturing cost.
本發明提供一種多孔性製氫材料,其包括由纖維組成的多孔性載體,因而具有良好的親水性以及堅固的多孔性結構。 The present invention provides a porous hydrogen producing material comprising a porous carrier composed of fibers, and thus having good hydrophilicity and a strong porous structure.
本發明再提供一種多孔性製氫材料的製造方法,其具有簡便的製造流程。 The present invention further provides a method for producing a porous hydrogen producing material, which has a simple manufacturing process.
本發明提出一種多孔性製氫材料,其包括一纖維載體、一製氫劑以及一熱熔劑。纖維載體包括多條彼此堆疊在一起的纖維,且纖維之間具有多個孔隙。製氫劑分散於纖維載體之纖維上。熱熔劑將纖維載體之纖維以及製氫劑黏著在一起。 The present invention provides a porous hydrogen producing material comprising a fibrous carrier, a hydrogen generating agent, and a hot melt. The fibrous carrier comprises a plurality of fibers stacked on each other with a plurality of pores between the fibers. The hydrogen generating agent is dispersed on the fibers of the fiber carrier. The hot melt adheres the fibers of the fiber carrier and the hydrogen generating agent together.
在本發明之一實施例中,上述之纖維載體包括離子型纖維載體。 In an embodiment of the invention, the fibrous carrier comprises an ionic fibrous carrier.
在本發明之一實施例中,上述之離子型纖維載體包括一天然水溶性聚合物載體、一改質天然聚合物載體或一合成聚合物載體。 In one embodiment of the invention, the ionic fibrous carrier comprises a natural water soluble polymeric carrier, a modified natural polymeric carrier or a synthetic polymeric carrier.
在本發明之一實施例中,上述之製氫劑包括NaBH4、NH3BH3、MgH2或C10H18。 In an embodiment of the invention, the hydrogen generating agent comprises NaBH 4 , NH 3 BH 3 , MgH 2 or C 10 H 18 .
在本發明之一實施例中,上述之熱熔劑包括聚乙烯(PE)、乙烯-醋酸乙烯酯(EVA)、聚胺基甲酸酯(TPU)或聚對苯二甲酸乙二酯(PET)。 In an embodiment of the invention, the hot melt comprises polyethylene (PE), ethylene vinyl acetate (EVA), polyurethane (TPU) or polyethylene terephthalate (PET). .
在本發明之一實施例中,上述之纖維載體、製氫劑以 及熱熔劑的重量比例為1.5:4:1.5。 In an embodiment of the invention, the fiber carrier and the hydrogen generating agent are And the weight ratio of hot melt is 1.5:4:1.5.
本發明再提出一種多孔性製氫材料的製造方法,其包括下述步驟。提供一纖維載體、一製氫劑以及一熱熔劑。將纖維載體、製氫劑以及熱熔劑均勻混合以形成一混合材料。將混合材料進行一熱處理程序以形成多孔性製氫材料。 The present invention further provides a method of producing a porous hydrogen producing material comprising the following steps. A fiber carrier, a hydrogen generator, and a hot melt are provided. The fibrous carrier, the hydrogen generating agent, and the hot melt are uniformly mixed to form a mixed material. The mixed material is subjected to a heat treatment process to form a porous hydrogen producing material.
在本發明之一實施例中,上述纖維載體的製造方法包括下述步驟。製備一纖維溶液。製備一含鈷凝固浴。將纖維溶液放入一紡絲裝置中以進行一紡織程序,其中紡織裝置將纖維溶液擠入至含鈷凝固浴中以機械抽絲方式形成長纖維。 In an embodiment of the invention, the method of manufacturing the fibrous carrier comprises the following steps. A fiber solution was prepared. A cobalt-containing coagulation bath was prepared. The fiber solution is placed in a spinning apparatus to perform a weaving process in which the spinning apparatus squeezes the fiber solution into a cobalt-containing coagulation bath to form long fibers by mechanical spinning.
在本發明之一實施例中,上述之纖維溶液包括離子型纖維溶液。 In an embodiment of the invention, the fiber solution comprises an ionic fiber solution.
在本發明之一實施例中,上述之離子型纖維溶液包括一天然水溶性聚合物溶液、一改質天然聚合物溶液或是一合成聚合物溶液。 In an embodiment of the invention, the ionic fiber solution comprises a natural water-soluble polymer solution, a modified natural polymer solution or a synthetic polymer solution.
在本發明之一實施例中,上述之天然水溶性聚合物溶液包括纖維素溶液、澱粉溶液、殼聚糖甲殼素溶液或海藻酸鈉溶液。上述之改質天然聚合物溶液包括改質澱粉溶液以及改質纖維素溶液,其中改質澱粉溶液包括羧甲基澱粉溶液或醋酸澱粉溶液,改質纖維素溶液包括羥甲基纖維素溶液或羧甲基纖維素溶液。上述之合成聚合物溶液包括具有陰離子基團的聚合類樹脂溶液或縮合類樹脂溶液,其中陰離子基團包括羧酸基、磺酸基、磷酸基或硫酸基。 In an embodiment of the invention, the above natural water-soluble polymer solution comprises a cellulose solution, a starch solution, a chitosan chitin solution or a sodium alginate solution. The modified natural polymer solution includes a modified starch solution and a modified cellulose solution, wherein the modified starch solution comprises a carboxymethyl starch solution or a starch acetate solution, and the modified cellulose solution comprises a hydroxymethyl cellulose solution or a carboxy group. Methylcellulose solution. The above synthetic polymer solution includes a polymer resin solution or a condensed resin solution having an anionic group, wherein the anionic group includes a carboxylic acid group, a sulfonic acid group, a phosphoric acid group or a sulfuric acid group.
在本發明之一實施例中,上述之纖維溶液的濃度為 2%~5%重量百分比。 In an embodiment of the invention, the concentration of the fiber solution is 2% to 5% by weight.
在本發明之一實施例中,上述之含鈷凝固浴包括氯化鈷凝固浴。 In an embodiment of the invention, the cobalt-containing coagulation bath comprises a cobalt chloride coagulation bath.
在本發明之一實施例中,上述之含鈷凝固浴的濃度為5%~55%重量百分比(室溫下飽和濃度),較佳的是,上述之含鈷凝固浴的濃度較佳為10%~25%。 In an embodiment of the present invention, the concentration of the cobalt-containing coagulation bath is 5% to 55% by weight (saturated concentration at room temperature), and preferably, the concentration of the cobalt-containing coagulation bath is preferably 10 %~25%.
在本發明之一實施例中,上述之製氫劑包括NaBH4、NH3BH3、MgH2或C10H18。 In an embodiment of the invention, the hydrogen generating agent comprises NaBH 4 , NH 3 BH 3 , MgH 2 or C 10 H 18 .
在本發明之一實施例中,上述之熱熔劑包括聚乙烯(PE)、乙烯-醋酸乙烯酯(EVA)、聚胺基甲酸酯(TPU)或聚對苯二甲酸乙二酯(PET)。 In an embodiment of the invention, the hot melt comprises polyethylene (PE), ethylene vinyl acetate (EVA), polyurethane (TPU) or polyethylene terephthalate (PET). .
在本發明之一實施例中,上述之熱處理程序包括下述步驟。將混合材料放置於一模具中。進行一壓模程序。進行一加熱定型程序。 In an embodiment of the invention, the heat treatment procedure described above comprises the steps described below. The mixed material is placed in a mold. Perform a compression molding process. Perform a heat setting procedure.
在本發明之一實施例中,上述之纖維載體、製氫劑以及熱熔劑的重量比例為1.5:4:1.5。 In one embodiment of the invention, the weight ratio of the above fibrous carrier, hydrogen generating agent and hot melt is 1.5:4:1.5.
基於上述,本發明之多孔性製氫材料包括親水性纖維載體,具有良好的親水性。此外,多孔性纖維載體中的孔隙可提供適當的空間讓水與製氫劑進行反應。另外,本發明之多孔性製氫材料具有足夠機械強度,其結構不易損壞。而且,本發明之多孔性製氫材料的製造方法具簡單製造的特性。 Based on the above, the porous hydrogen producing material of the present invention comprises a hydrophilic fibrous carrier and has good hydrophilicity. In addition, the pores in the porous fibrous support provide a suitable space for the water to react with the hydrogen generating agent. Further, the porous hydrogen producing material of the present invention has sufficient mechanical strength and its structure is not easily damaged. Further, the method for producing a porous hydrogen producing material of the present invention has a property of being simple to manufacture.
為讓本發明之上述特徵和優點能更明顯易懂,下文特舉實施例,並配合所附圖式作詳細說明如下。 The above described features and advantages of the present invention will be more apparent from the following description.
圖1是本發明一實施例之多孔性製氫材料的製造方法的流程示意圖。請參考圖1,首先進行步驟S10,提供一纖維載體、一製氫劑以及一熱熔劑。其中,纖維載體、製氫劑與熱熔劑的重量比例例如為1.5:4:1.5。纖維載體包括多條彼此堆疊在一起的纖維,且纖維載體例如是一離子型纖維載體,特別的是,離子型纖維具有親水的特性。上述離子型纖維載體例如是一天然水溶性聚合物載體、一改質天然聚合物載體或是一合成聚合物載體。此外,上述製氫劑例如是NaBH4、NH3BH3、MgH2或C10H18。上述熱熔劑例如是聚乙烯(PE)、乙烯-醋酸乙烯酯(EVA)、聚胺基甲酸酯(TPU)或聚對苯二甲酸乙二酯(PET),在此列出熱熔劑的化合物僅為舉例說明。一般來說,只要是低熔點的高分子化合物皆可使用,本發明不以此為限。 BRIEF DESCRIPTION OF THE DRAWINGS Fig. 1 is a flow chart showing a method of producing a porous hydrogen producing material according to an embodiment of the present invention. Referring to FIG. 1, first, step S10 is performed to provide a fiber carrier, a hydrogen generating agent, and a hot melt. The weight ratio of the fibrous carrier, the hydrogen generating agent and the hot melt is, for example, 1.5:4:1.5. The fibrous carrier comprises a plurality of fibers stacked on each other, and the fibrous carrier is, for example, an ionic fibrous carrier, and in particular, the ionic fibers have hydrophilic properties. The above ionic fiber carrier is, for example, a natural water-soluble polymer carrier, a modified natural polymer carrier or a synthetic polymer carrier. Further, the above hydrogen generating agent is, for example, NaBH 4 , NH 3 BH 3 , MgH 2 or C 10 H 18 . The above hot melt agent is, for example, polyethylene (PE), ethylene vinyl acetate (EVA), polyurethane (TPU) or polyethylene terephthalate (PET), and the hot melt compound is listed here. Just for illustration. In general, any polymer compound having a low melting point can be used, and the present invention is not limited thereto.
接著,進行步驟S20,將上述的纖維載體、製氫劑以及熱熔劑均勻混合後形成一混合材料。 Next, in step S20, the above-mentioned fibrous carrier, hydrogen generating agent and hot melt are uniformly mixed to form a mixed material.
最後,進行步驟S30,將上述的混合材料進行一熱處理程序以形成多孔性製氫材料100。詳細而言,圖2A至圖2D為步驟S30中熱處理程序的製造流程示意圖。請參考圖2A至圖2D,首先,將包括上述纖維載體120、製氫劑140以及熱熔劑160的混合材料X放置於一模具A中,如圖2A所示。接著,如圖2B所示進行一壓模程序P1以及如圖2C所示進行一加熱定型程序P2。最後,將模具A移 除,即可完成多孔性製氫材料100的製作,如圖2D所示。具體而言,壓模程序P1可以將混合材料壓縮成一塊狀固體。接著,進行加熱定型程序P2時,熱熔劑160會隨著溫度升高而熔化成液體狀態,此時,液態的熱熔劑160會散佈在纖維122以及製氫劑140之間。然後,進行降溫的動作,液態的熱熔劑160就會固化,而把製氫劑140以及纖維122黏在一起。需說明的是,因為熱熔劑160於液體狀態時,不會填滿所有位於纖維122與製氫劑140之間的空間,因此固化後會形成具有空隙的形態。 Finally, in step S30, the above mixed material is subjected to a heat treatment process to form the porous hydrogen producing material 100. In detail, FIGS. 2A to 2D are schematic views showing a manufacturing flow of the heat treatment procedure in step S30. Referring to FIGS. 2A to 2D, first, a mixed material X including the above-described fiber carrier 120, hydrogen generating agent 140, and hot melt 160 is placed in a mold A as shown in FIG. 2A. Next, a stamper P1 is performed as shown in Fig. 2B and a heat setting program P2 is performed as shown in Fig. 2C. Finally, move the mold A Alternatively, the fabrication of the porous hydrogen production material 100 can be accomplished, as shown in Figure 2D. Specifically, the molding process P1 can compress the mixed material into a piece of solid. Next, when the heating setting program P2 is performed, the hot melt 160 is melted into a liquid state as the temperature rises, and at this time, the liquid hot melt 160 is interspersed between the fibers 122 and the hydrogen generating agent 140. Then, the cooling action is performed, and the liquid hot melt 160 is solidified, and the hydrogen generating agent 140 and the fibers 122 are adhered together. It should be noted that since the hot melt 160 does not fill all the spaces between the fibers 122 and the hydrogen generating agent 140 in the liquid state, a form having voids is formed after curing.
在此說明上述纖維載體120的製造方法,其包括下述的步驟。首先,製備一纖維溶液。接著,製備一含鈷凝固浴。最後,將纖維溶液放入一紡絲裝置中以進行一紡織程序,其中紡絲裝置將纖維溶液擠入至含鈷凝固浴中以機械抽絲方式形成長纖維。上述紡織製程例如為濕式紡織製程。 Here, a method of manufacturing the above fiber carrier 120 will be described, which includes the following steps. First, a fiber solution is prepared. Next, a cobalt-containing coagulation bath was prepared. Finally, the fiber solution is placed in a spinning apparatus to perform a weaving process in which the spinning apparatus extrudes the fiber solution into a cobalt-containing coagulation bath to form long fibers by mechanical spinning. The above textile process is, for example, a wet textile process.
具體來說,纖維溶液的濃度例如為2%至5%重量百分比。在此說明的是,纖維溶液中包括溶質以及溶劑,上述的濃度是指溶質於溶液中的重量百分比濃度。詳細而言,纖維溶液例如是離子型纖維溶液,且離子型纖維溶液例如是一天然水溶性聚合物溶液、一改質天然聚合物溶液或是一合成聚合物溶液。其中,上述天然水溶性聚合物溶液例如是纖維素溶液、澱粉溶液、殼聚糖甲殼素溶液或海藻酸鈉溶液。上述改質天然聚合物例如是改質澱粉溶液以及改質纖維素溶液,其中改質澱粉溶液例如是羧甲基澱粉溶液或醋酸澱粉溶液,而改質纖維素溶液例如是羥甲基纖維素 溶液或羧甲基纖維素溶液。上述合成聚合物溶液例如是具有陰離子基團的聚合類樹脂或縮合類樹脂溶液,其中上述陰離子基團例如是羧酸基、礦酸基、磷酸基或硫酸基。另外,上述的含鈷凝固浴例如為氯化鈷凝固浴。含鈷凝固浴的濃度例如為5%至55%重量百分比(室溫下飽和濃度)。在此說明的是,含鈷凝固浴包括溶質以及溶劑,上述的濃度是指溶質於溶液中的重量百分比濃度。 Specifically, the concentration of the fiber solution is, for example, 2% to 5% by weight. It is explained herein that the fiber solution includes a solute and a solvent, and the above concentration refers to a concentration by weight of the solute in the solution. In detail, the fiber solution is, for example, an ionic fiber solution, and the ionic fiber solution is, for example, a natural water-soluble polymer solution, a modified natural polymer solution, or a synthetic polymer solution. Wherein, the above natural water-soluble polymer solution is, for example, a cellulose solution, a starch solution, a chitosan chitin solution or a sodium alginate solution. The modified natural polymer is, for example, a modified starch solution and a modified cellulose solution, wherein the modified starch solution is, for example, a carboxymethyl starch solution or a starch acetate solution, and the modified cellulose solution is, for example, hydroxymethyl cellulose. Solution or carboxymethylcellulose solution. The above synthetic polymer solution is, for example, a polymer-based resin or a condensed resin solution having an anionic group such as a carboxylic acid group, a mineral acid group, a phosphoric acid group or a sulfuric acid group. Further, the above cobalt-containing coagulation bath is, for example, a cobalt chloride coagulation bath. The concentration of the cobalt-containing coagulation bath is, for example, 5% to 55% by weight (saturated concentration at room temperature). It is explained herein that the cobalt-containing coagulation bath includes a solute and a solvent, and the above concentration refers to a concentration by weight of the solute in the solution.
詳細的來說,當纖維溶液擠入至含鈷凝固浴時,含鈷凝固浴中的鈷離子會與纖維溶液中的纖維溶質產生離子鍵結,而使原本為水溶性的纖維溶質變成非水溶性的固化纖維。因此,鈷離子會以離子鍵鍵結至纖維的表面。 In detail, when the fiber solution is extruded into the cobalt-containing coagulation bath, the cobalt ions in the cobalt-containing coagulation bath are ionically bonded to the fiber solute in the fiber solution, and the otherwise water-soluble fiber solute becomes non-water soluble. Sexual curing fiber. Therefore, cobalt ions are ionic bonded to the surface of the fiber.
至此,便完成多孔性製氫材料100的製作。亦即,只需進行步驟S10至步驟S30即可完成本發明之多孔性製氫材料100的製作,因此本發明之製氫材料100的製造方法具有簡單的製造流程。更值得一提的是,除了上述塊狀的形態之外,技術人員更可以依照其實際需求,更換不同形狀的模具,即可以得到不同形狀的多孔性製氫材料,因此,本發明之多孔性製氫材料100的製造方法適於實際應用。 Thus, the production of the porous hydrogen producing material 100 is completed. That is, the production of the porous hydrogen producing material 100 of the present invention can be completed by performing only steps S10 to S30. Therefore, the method for producing the hydrogen producing material 100 of the present invention has a simple manufacturing process. What is more worth mentioning is that, in addition to the above-mentioned block shape, the technician can change the mold of different shapes according to the actual needs thereof, that is, the porous hydrogen production material of different shapes can be obtained, and therefore, the porosity of the present invention The method of manufacturing the hydrogen producing material 100 is suitable for practical use.
圖3是本發明一實施例之多孔性製氫材料100的結構示意圖。圖4是圖3中局部區域M的放大平面示意圖。請參照圖3以及圖4,本實施例之多孔性製氫材料100包括一纖維載體120、一製氫劑140以及一熱熔劑160。其中纖維載體120包括多條彼此堆疊在一起的纖維122,且纖維122之間具有多個孔隙124。換言之,當纖維122彼此堆疊 時,纖維122彼此之間構成了孔隙,亦即形成一立體空間。纖維載體120例如是一離子型纖維載體。上述離子型纖維載體例如是一天然水溶性聚合物載體、一改質天然聚合物或是一合成聚合物載體。並且,纖維載體120具有良好的親水性質。 Fig. 3 is a schematic view showing the structure of a porous hydrogen producing material 100 according to an embodiment of the present invention. 4 is an enlarged plan view showing a partial area M of FIG. 3. Referring to FIG. 3 and FIG. 4, the porous hydrogen production material 100 of the present embodiment includes a fiber carrier 120, a hydrogen generating agent 140, and a hot melt 160. The fiber carrier 120 includes a plurality of fibers 122 stacked on one another with a plurality of apertures 124 between the fibers 122. In other words, when the fibers 122 are stacked on each other At the same time, the fibers 122 form a void with each other, that is, form a three-dimensional space. The fiber carrier 120 is, for example, an ionic fiber carrier. The above ionic fiber carrier is, for example, a natural water-soluble polymer carrier, a modified natural polymer or a synthetic polymer carrier. Also, the fiber carrier 120 has good hydrophilic properties.
製氫劑140分散於纖維載體120之纖維122上。詳言之,製氫劑140會散佈在纖維122之間的孔隙,亦即部分製氫劑140位於纖維122堆疊後所形成的立體空間中。 The hydrogen generating agent 140 is dispersed on the fibers 122 of the fiber carrier 120. In particular, the hydrogen generating agent 140 is interspersed with pores between the fibers 122, that is, a portion of the hydrogen generating agent 140 is located in the three-dimensional space formed by the stacking of the fibers 122.
熱熔劑160將纖維載體120之纖維122以及製氫劑140黏著在一起。詳細而言,熱熔劑160例如是低熔點高分子,藉由加熱定型程序可以讓纖維載體120與製氫劑140形成多孔性的塊狀固體。而且,此塊狀固體可以具有一定的強度。不易在產氫之後,產生結構崩解的問題。 The hot melt 160 adheres the fibers 122 of the fiber carrier 120 and the hydrogen generating agent 140 together. In detail, the hot melt 160 is, for example, a low melting point polymer, and the fiber carrier 120 and the hydrogen generating agent 140 can form a porous bulk solid by a heat setting process. Moreover, the bulk solid can have a certain strength. It is not easy to cause the problem of structural disintegration after hydrogen production.
為了詳細說明本發明之多孔性製氫材料,以下將介紹一實例的製造流程。首先,進行纖維載體的製作。表一為此實例於紡絲時之相關實驗條件。 In order to explain in detail the porous hydrogen producing material of the present invention, an example of the manufacturing process will be described below. First, the production of the fiber carrier is carried out. Table 1 shows the relevant experimental conditions for spinning in this example.
請參考表一,以濃度為2%重量百分比的海藻酸鈉溶液作為纖維溶液,將海藻酸鈉溶液放置在紡織裝置中並將其擠入至濃度為25%重量百分比的氯化鈷凝固浴中,此時水溶性的海藻酸鈉分子中的鈉離子會與凝固浴中的鈷離子交換形成離子鍵結,並形成固化的海藻酸鈷纖維,並完成纖維載體的製作。此海藻酸鈷纖維為非水溶性且具有親水性(吸水性)。更詳細來說,可在海藻酸鈷纖維形成後,再次將其含浸到凝固浴約12小時,以增加海藻酸鈷纖維的含鈷量。 Referring to Table 1, a sodium alginate solution having a concentration of 2% by weight is used as a fiber solution, and the sodium alginate solution is placed in a spinning device and extruded into a cobalt chloride coagulation bath at a concentration of 25% by weight. At this time, the sodium ions in the water-soluble sodium alginate molecule exchange ion exchange with the cobalt ions in the coagulation bath to form a solidified cobalt alginate fiber, and the fiber carrier is completed. This cobalt alginate fiber is water-insoluble and hydrophilic (water absorption). More specifically, after the cobalt alginate fibers are formed, they are again impregnated into the coagulation bath for about 12 hours to increase the cobalt content of the cobalt alginate fibers.
接著,以硼氫化鈉(NaBH4)為製氫劑,以高密度聚乙烯(HDPE)為熱熔劑。將海藻酸鈷纖維、硼氫化鈉以及高密度聚乙烯(HDPE)依照重量比例為1.5:4:1.5的比例混合成混合材料。再將此混合材料放於模具中進行壓模以及加熱定型程序。其中,使用模具加熱定型的溫度為150℃,時間為2小時,即可形成海藻酸鈷纖維之間具有多個孔隙的結構,且製氫劑分散於海藻酸鈷纖維上,並完成此實例之多孔性製氫材料。 Next, sodium borohydride (NaBH 4 ) was used as a hydrogen generator, and high density polyethylene (HDPE) was used as a hot melt. The cobalt alginate fiber, sodium borohydride, and high density polyethylene (HDPE) were mixed into a mixed material in a ratio of 1.5:4:1.5 by weight. The mixed material is placed in a mold for compression molding and a heat setting process. Wherein, using a mold for heating and setting at a temperature of 150 ° C for 2 hours, a structure having a plurality of pores between the cobalt alginate fibers is formed, and the hydrogen generating agent is dispersed on the cobalt alginate fibers, and the example is completed. Porous hydrogen production material.
特別說明的是,本發明之多孔性製氫材料的使用方法為直接將水加入多孔性製氫材料中。由於多孔性製氫材料中具有由海藻酸鈷纖維所支撐形成的孔隙,硼氫化鈉附著於海藻酸鈷纖維之上,且海藻酸鈷纖維中的鈷離子可以作為觸媒。因此,當水進入孔隙中,孔隙便提供一個空間結構讓水與硼氫化鈉反應,且鈷離子有利於催化反應的進行 而產生氫氣。此外,由於海藻酸鈷纖維的吸水/含水率非常的高,因此有利於將水分留在纖維載體上,以提升產氫效率。另外,高密度聚乙烯(HDPE)的使用可以提供多孔性製氫材料具有足夠的機械強度,因此,當氫氣產生並由孔隙中冒出之時,本發明之多孔性製氫材料不易產生結構崩解的情形。 In particular, the porous hydrogen producing material of the present invention is used by directly adding water to the porous hydrogen producing material. Since the porous hydrogen producing material has pores supported by cobalt alginate fibers, sodium borohydride adheres to the cobalt alginate fibers, and cobalt ions in the cobalt alginate fibers can serve as a catalyst. Therefore, when water enters the pores, the pores provide a spatial structure for the water to react with sodium borohydride, and the cobalt ions facilitate the catalytic reaction. Hydrogen is produced. In addition, since the water absorption/water content of the cobalt alginate fiber is very high, it is advantageous to leave moisture on the fiber carrier to improve the hydrogen production efficiency. In addition, the use of high-density polyethylene (HDPE) can provide a porous hydrogen-producing material with sufficient mechanical strength, so that when hydrogen is generated and emerges from the pores, the porous hydrogen-producing material of the present invention is less prone to structural collapse. The situation of the solution.
承上述,為詳細說明硼氫化鈉、海藻酸鈷纖維以及熱熔粉之含量比例對於多孔性製氫材料之影響,於表二中特舉具有不同含量比例之比較例1以及比較例2為例說明。 In view of the above, in order to explain in detail the influence of the content ratio of sodium borohydride, cobalt alginate fiber and hot-melt powder on the porous hydrogen-producing material, Comparative Example 1 and Comparative Example 2 which have different content ratios in Table 2 are exemplified. Description.
請參考表二,比較例1以及比較例2之多孔性製氫材料中的熱熔粉含量較實例之多孔性製氫材料低。進行給水測試時,比較例1以及比較例2之多孔性製氫材料在氫氣產生之後,其結構因此而崩塌。而實例之多孔性製氫材料則維持完整的結構。由此可知,當海藻酸鈷纖維、硼氫化鈉以及熱熔粉的含量比例實質上為1.5:4:1.5時,多孔性製氫材料即可具有足夠的機械強度以維持製氫時的多孔性結構。 Referring to Table 2, the content of the hot-melt powder in the porous hydrogen-producing material of Comparative Example 1 and Comparative Example 2 was lower than that of the example porous hydrogen-producing material. When the water supply test was performed, the porous hydrogen production materials of Comparative Example 1 and Comparative Example 2 collapsed after the generation of hydrogen gas. The example of a porous hydrogen production material maintains a complete structure. It can be seen that when the content ratio of cobalt alginate fiber, sodium borohydride and hot-melt powder is substantially 1.5:4:1.5, the porous hydrogen-producing material can have sufficient mechanical strength to maintain porosity during hydrogen production. structure.
更值得一提的是,當硼氫化鈉與水反應後,會與海藻 酸鈷纖維中的鈷離子形成鈷硼觸媒,鈷硼觸媒可以進一步用來催化硼氫化鈉與水反應產生氫氣。換言之,當本發明之製氫劑使用含硼之化合物時,例如為硼氫化鈉(NaBH4)或硼氫化氨(NH3BH3),則本發明之多孔性製氫材料可以是逐步性的催化反應,因而具有二段式的製氫反應,亦即長效性的製氫效能。此外,因為鈷硼觸媒形成後會附著於纖維之表面,且其不易隨著水分流失,因此可以提高產氫的效率。此外,因為本發明之多孔性製氫材料具有良好的機械強度,其在製氫之後結構不易損壞,因此鈷硼觸媒可以再次回收利用。 It is worth mentioning that when sodium borohydride reacts with water, it forms a cobalt boron catalyst with cobalt ions in the cobalt alginate fiber. The cobalt boron catalyst can be further used to catalyze the reaction of sodium borohydride with water to generate hydrogen. In other words, when the hydrogen-generating agent of the present invention uses a boron-containing compound such as sodium borohydride (NaBH 4 ) or borohydride (NH 3 BH 3 ), the porous hydrogen-generating material of the present invention may be stepwise. Catalytic reaction, thus having a two-stage hydrogen production reaction, that is, long-term hydrogen production efficiency. In addition, since the cobalt-boron catalyst adheres to the surface of the fiber after formation, it is not easily lost with water, so that the efficiency of hydrogen production can be improved. Further, since the porous hydrogen producing material of the present invention has good mechanical strength, its structure is not easily damaged after hydrogen production, and therefore the cobalt boron catalyst can be recycled again.
當然,上述有關多孔性製氫材料詳細的合成流程以及各種材料之濃度以及用量,僅為讓此領域之技術人員能夠據以實施,並非用於限定本發明。 Of course, the detailed synthetic procedure for the porous hydrogen-producing material described above, as well as the concentration and amount of various materials, are only intended to enable those skilled in the art to practice the invention and are not intended to limit the invention.
綜上所述,本發明之多孔性製氫材料包括由親水性纖維組成的多孔性纖維載體,因而其具有良好的親水性並提供適當的空間讓水與製氫劑進行反應。此外,熱熔劑的使用可以讓多孔性製氫材料且有足夠的機械強度,其結構不易損壞。再者,附著於纖維表面上的鈷離子以及可能形成的鈷硼離子更可以提供二段式催化製氫效能。因此,本發明之多孔性製氫材料具有長效性催化製氫效能。此外本發明之多孔性製氫材料的製造方法相當的簡單且方便製作。 As described above, the porous hydrogen producing material of the present invention comprises a porous fibrous carrier composed of hydrophilic fibers, so that it has good hydrophilicity and provides a suitable space for the water to react with the hydrogen generating agent. In addition, the use of a hot melt allows the porous hydrogen producing material to have sufficient mechanical strength and its structure is not easily damaged. Furthermore, cobalt ions attached to the surface of the fiber and possibly cobalt boron ions can provide a two-stage catalytic hydrogen production efficiency. Therefore, the porous hydrogen producing material of the present invention has a long-acting catalytic hydrogen production efficiency. Further, the method for producing a porous hydrogen producing material of the present invention is relatively simple and convenient to produce.
雖然本發明已以實施例揭露如上,然其並非用以限定本發明,任何所屬技術領域中具有通常知識者,在不脫離本發明之精神和範圍內,當可作些許之更動與潤飾,故本 發明之保護範圍當視後附之申請專利範圍所界定者為準。 Although the present invention has been disclosed in the above embodiments, it is not intended to limit the invention, and any one of ordinary skill in the art can make some modifications and refinements without departing from the spirit and scope of the invention. this The scope of the invention is defined by the scope of the appended claims.
S10、S20、S30‧‧‧步驟 S10, S20, S30‧‧‧ steps
100‧‧‧多孔性製氫材料 100‧‧‧Porous hydrogen production materials
120‧‧‧纖維載體 120‧‧‧Fiber carrier
122‧‧‧纖維 122‧‧‧ fiber
124‧‧‧孔隙 124‧‧‧ pores
140‧‧‧製氫劑 140‧‧‧ Hydrogen generator
160‧‧‧熱熔劑 160‧‧‧Hot flux
X‧‧‧混合材料 X‧‧‧ mixed materials
P1‧‧‧壓模程序 P1‧‧‧ compression molding program
P2‧‧‧加熱定型程序 P2‧‧‧heat setting procedure
M‧‧‧區域 M‧‧‧ area
圖1是本發明一實施例之多孔性製氫材料的製造方法的流程示意圖。 BRIEF DESCRIPTION OF THE DRAWINGS Fig. 1 is a flow chart showing a method of producing a porous hydrogen producing material according to an embodiment of the present invention.
圖2A至圖2D為熱處理程序的製造流程示意圖。 2A to 2D are schematic views showing a manufacturing process of a heat treatment process.
圖3是本發明一實施例之多孔性製氫材料的結構示意圖。 Fig. 3 is a schematic view showing the structure of a porous hydrogen producing material according to an embodiment of the present invention.
圖4是圖3中局部區域M的放大平面示意圖。 4 is an enlarged plan view showing a partial area M of FIG. 3.
100‧‧‧多孔性製氫材料 100‧‧‧Porous hydrogen production materials
120‧‧‧纖維載體 120‧‧‧Fiber carrier
122‧‧‧纖維 122‧‧‧ fiber
124‧‧‧孔隙 124‧‧‧ pores
160‧‧‧熱熔劑 160‧‧‧Hot flux
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| CN1845873A (en) * | 2003-08-14 | 2006-10-11 | 吉莱特公司 | Hydrogen generator |
| CN1936120A (en) * | 2006-10-20 | 2007-03-28 | 北京服装学院 | A method for preparing ion exchange fibers by solution electrospinning |
| CN1990540A (en) * | 2005-12-30 | 2007-07-04 | 上海杰事杰新材料股份有限公司 | Fiber reinforced thermolplastic composite material preparation method |
| CN101100285A (en) * | 2006-07-07 | 2008-01-09 | 中国科学院金属研究所 | Chemical hydride hydrogen storage material system, hydrogen production method and hydrogen production device |
| CN101203305A (en) * | 2005-06-29 | 2008-06-18 | 三星工程株式会社 | Metal oxide catalyst for producing hydrogen and method for preparing the metal oxide catalyst |
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| Publication number | Priority date | Publication date | Assignee | Title |
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| CN1845873A (en) * | 2003-08-14 | 2006-10-11 | 吉莱特公司 | Hydrogen generator |
| CN101203305A (en) * | 2005-06-29 | 2008-06-18 | 三星工程株式会社 | Metal oxide catalyst for producing hydrogen and method for preparing the metal oxide catalyst |
| CN1990540A (en) * | 2005-12-30 | 2007-07-04 | 上海杰事杰新材料股份有限公司 | Fiber reinforced thermolplastic composite material preparation method |
| CN101100285A (en) * | 2006-07-07 | 2008-01-09 | 中国科学院金属研究所 | Chemical hydride hydrogen storage material system, hydrogen production method and hydrogen production device |
| CN1936120A (en) * | 2006-10-20 | 2007-03-28 | 北京服装学院 | A method for preparing ion exchange fibers by solution electrospinning |
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