CN109972010B - Nano magnesium-based composite hydrogen storage material and preparation method thereof - Google Patents
Nano magnesium-based composite hydrogen storage material and preparation method thereof Download PDFInfo
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- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 title claims abstract description 107
- 239000001257 hydrogen Substances 0.000 title claims abstract description 107
- 229910052739 hydrogen Inorganic materials 0.000 title claims abstract description 107
- 239000011777 magnesium Substances 0.000 title claims abstract description 60
- 229910052749 magnesium Inorganic materials 0.000 title claims abstract description 59
- FYYHWMGAXLPEAU-UHFFFAOYSA-N Magnesium Chemical compound [Mg] FYYHWMGAXLPEAU-UHFFFAOYSA-N 0.000 title claims abstract description 57
- 239000011232 storage material Substances 0.000 title claims abstract description 39
- 239000002131 composite material Substances 0.000 title claims abstract description 33
- 238000002360 preparation method Methods 0.000 title claims abstract description 21
- 239000000463 material Substances 0.000 claims abstract description 72
- 229910052761 rare earth metal Inorganic materials 0.000 claims abstract description 57
- 238000010521 absorption reaction Methods 0.000 claims abstract description 49
- 229910045601 alloy Inorganic materials 0.000 claims abstract description 40
- 239000000956 alloy Substances 0.000 claims abstract description 40
- PXHVJJICTQNCMI-UHFFFAOYSA-N Nickel Chemical compound [Ni] PXHVJJICTQNCMI-UHFFFAOYSA-N 0.000 claims abstract description 35
- 238000000498 ball milling Methods 0.000 claims abstract description 33
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims abstract description 27
- 150000002910 rare earth metals Chemical class 0.000 claims abstract description 22
- 238000000227 grinding Methods 0.000 claims abstract description 19
- 238000003723 Smelting Methods 0.000 claims abstract description 13
- 229910002804 graphite Inorganic materials 0.000 claims abstract description 13
- 239000010439 graphite Substances 0.000 claims abstract description 13
- 230000006698 induction Effects 0.000 claims abstract description 9
- 239000003054 catalyst Substances 0.000 claims abstract description 5
- 238000000034 method Methods 0.000 claims description 29
- 239000000843 powder Substances 0.000 claims description 13
- XKRFYHLGVUSROY-UHFFFAOYSA-N Argon Chemical compound [Ar] XKRFYHLGVUSROY-UHFFFAOYSA-N 0.000 claims description 12
- IMNFDUFMRHMDMM-UHFFFAOYSA-N N-Heptane Chemical compound CCCCCCC IMNFDUFMRHMDMM-UHFFFAOYSA-N 0.000 claims description 9
- 239000007788 liquid Substances 0.000 claims description 9
- 239000002245 particle Substances 0.000 claims description 9
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 claims description 7
- 238000002844 melting Methods 0.000 claims description 7
- 230000008018 melting Effects 0.000 claims description 7
- UHOVQNZJYSORNB-UHFFFAOYSA-N Benzene Chemical compound C1=CC=CC=C1 UHOVQNZJYSORNB-UHFFFAOYSA-N 0.000 claims description 6
- WYURNTSHIVDZCO-UHFFFAOYSA-N Tetrahydrofuran Chemical compound C1CCOC1 WYURNTSHIVDZCO-UHFFFAOYSA-N 0.000 claims description 6
- YXFVVABEGXRONW-UHFFFAOYSA-N Toluene Chemical compound CC1=CC=CC=C1 YXFVVABEGXRONW-UHFFFAOYSA-N 0.000 claims description 6
- 229910052786 argon Inorganic materials 0.000 claims description 6
- 239000007789 gas Substances 0.000 claims description 6
- VLKZOEOYAKHREP-UHFFFAOYSA-N n-Hexane Chemical compound CCCCCC VLKZOEOYAKHREP-UHFFFAOYSA-N 0.000 claims description 6
- 229910052759 nickel Inorganic materials 0.000 claims description 6
- 239000002994 raw material Substances 0.000 claims description 5
- 229910052684 Cerium Inorganic materials 0.000 claims description 3
- 229910052779 Neodymium Inorganic materials 0.000 claims description 3
- 229910052777 Praseodymium Inorganic materials 0.000 claims description 3
- 229910052772 Samarium Inorganic materials 0.000 claims description 3
- 239000012535 impurity Substances 0.000 claims description 3
- 229910052746 lanthanum Inorganic materials 0.000 claims description 3
- FZLIPJUXYLNCLC-UHFFFAOYSA-N lanthanum atom Chemical compound [La] FZLIPJUXYLNCLC-UHFFFAOYSA-N 0.000 claims description 3
- QEFYFXOXNSNQGX-UHFFFAOYSA-N neodymium atom Chemical compound [Nd] QEFYFXOXNSNQGX-UHFFFAOYSA-N 0.000 claims description 3
- PUDIUYLPXJFUGB-UHFFFAOYSA-N praseodymium atom Chemical compound [Pr] PUDIUYLPXJFUGB-UHFFFAOYSA-N 0.000 claims description 3
- 230000001681 protective effect Effects 0.000 claims description 3
- KZUNJOHGWZRPMI-UHFFFAOYSA-N samarium atom Chemical compound [Sm] KZUNJOHGWZRPMI-UHFFFAOYSA-N 0.000 claims description 3
- YLQBMQCUIZJEEH-UHFFFAOYSA-N tetrahydrofuran Natural products C=1C=COC=1 YLQBMQCUIZJEEH-UHFFFAOYSA-N 0.000 claims description 3
- 239000000155 melt Substances 0.000 claims description 2
- 238000005266 casting Methods 0.000 claims 1
- GWXLDORMOJMVQZ-UHFFFAOYSA-N cerium Chemical compound [Ce] GWXLDORMOJMVQZ-UHFFFAOYSA-N 0.000 claims 1
- 238000001035 drying Methods 0.000 claims 1
- 238000002156 mixing Methods 0.000 claims 1
- 239000002159 nanocrystal Substances 0.000 claims 1
- 238000004321 preservation Methods 0.000 claims 1
- 238000003860 storage Methods 0.000 abstract description 14
- 238000011084 recovery Methods 0.000 abstract description 10
- 238000011065 in-situ storage Methods 0.000 abstract description 3
- 241001062472 Stokellia anisodon Species 0.000 abstract 1
- 230000008569 process Effects 0.000 description 19
- 238000003795 desorption Methods 0.000 description 8
- 230000000694 effects Effects 0.000 description 6
- 239000007787 solid Substances 0.000 description 6
- 230000004913 activation Effects 0.000 description 5
- 238000006555 catalytic reaction Methods 0.000 description 5
- 150000002431 hydrogen Chemical class 0.000 description 5
- 239000000203 mixture Substances 0.000 description 5
- 238000010586 diagram Methods 0.000 description 4
- 230000002441 reversible effect Effects 0.000 description 4
- 230000002195 synergetic effect Effects 0.000 description 4
- 238000012876 topography Methods 0.000 description 4
- XDTMQSROBMDMFD-UHFFFAOYSA-N Cyclohexane Chemical compound C1CCCCC1 XDTMQSROBMDMFD-UHFFFAOYSA-N 0.000 description 3
- 230000008901 benefit Effects 0.000 description 3
- 238000006243 chemical reaction Methods 0.000 description 3
- 239000011159 matrix material Substances 0.000 description 3
- CPLXHLVBOLITMK-UHFFFAOYSA-N Magnesium oxide Chemical compound [Mg]=O CPLXHLVBOLITMK-UHFFFAOYSA-N 0.000 description 2
- 230000003197 catalytic effect Effects 0.000 description 2
- ZMIGMASIKSOYAM-UHFFFAOYSA-N cerium Chemical compound [Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce] ZMIGMASIKSOYAM-UHFFFAOYSA-N 0.000 description 2
- 239000013078 crystal Substances 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 238000005984 hydrogenation reaction Methods 0.000 description 2
- 238000005461 lubrication Methods 0.000 description 2
- 229910052751 metal Inorganic materials 0.000 description 2
- 239000002184 metal Substances 0.000 description 2
- 229910052987 metal hydride Inorganic materials 0.000 description 2
- 150000004681 metal hydrides Chemical class 0.000 description 2
- 238000001291 vacuum drying Methods 0.000 description 2
- 229910001018 Cast iron Inorganic materials 0.000 description 1
- 229910001122 Mischmetal Inorganic materials 0.000 description 1
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 1
- 230000009471 action Effects 0.000 description 1
- 238000005054 agglomeration Methods 0.000 description 1
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- 239000012752 auxiliary agent Substances 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 239000011362 coarse particle Substances 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 238000006356 dehydrogenation reaction Methods 0.000 description 1
- 238000011161 development Methods 0.000 description 1
- 239000006185 dispersion Substances 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 238000002474 experimental method Methods 0.000 description 1
- 239000010419 fine particle Substances 0.000 description 1
- 239000000446 fuel Substances 0.000 description 1
- 238000000713 high-energy ball milling Methods 0.000 description 1
- 229910000765 intermetallic Inorganic materials 0.000 description 1
- 230000001050 lubricating effect Effects 0.000 description 1
- 239000000395 magnesium oxide Substances 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000003960 organic solvent Substances 0.000 description 1
- 230000000704 physical effect Effects 0.000 description 1
- 238000000746 purification Methods 0.000 description 1
- 238000011160 research Methods 0.000 description 1
- 238000010008 shearing Methods 0.000 description 1
- 239000010935 stainless steel Substances 0.000 description 1
- 229910001220 stainless steel Inorganic materials 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 238000012360 testing method Methods 0.000 description 1
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- C—CHEMISTRY; METALLURGY
- C22—METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
- C22C—ALLOYS
- C22C1/00—Making non-ferrous alloys
- C22C1/04—Making non-ferrous alloys by powder metallurgy
- C22C1/05—Mixtures of metal powder with non-metallic powder
-
- C—CHEMISTRY; METALLURGY
- C22—METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
- C22C—ALLOYS
- C22C23/00—Alloys based on magnesium
- C22C23/06—Alloys based on magnesium with a rare earth metal as the next major constituent
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M4/00—Electrodes
- H01M4/02—Electrodes composed of, or comprising, active material
- H01M4/36—Selection of substances as active materials, active masses, active liquids
- H01M4/38—Selection of substances as active materials, active masses, active liquids of elements or alloys
- H01M4/383—Hydrogen absorbing alloys
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M4/00—Electrodes
- H01M4/02—Electrodes composed of, or comprising, active material
- H01M4/36—Selection of substances as active materials, active masses, active liquids
- H01M4/38—Selection of substances as active materials, active masses, active liquids of elements or alloys
- H01M4/46—Alloys based on magnesium or aluminium
- H01M4/466—Magnesium based
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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
- Y02E60/10—Energy storage using batteries
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- General Chemical & Material Sciences (AREA)
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Abstract
本发明为一种纳米镁基复合储氢材料及其制备方法。材料主要成分为镁,同时包含混合稀土、羰基镍粉和石墨多种催化剂,以提升其低温吸氢性能。该材料具有纳米晶体结构,晶粒尺寸为20‑50纳米,且具有优异的低温吸氢动力学性能。制备方法中,首先采用真空感应熔炼方法将纯镁与一定量的混合稀土进行真空冶炼,制备出镁原位掺杂稀土元素的脆性镁‑稀土合金锭;然后将得到的合金与羰基镍粉、石墨粉、惰性有机助磨剂混合,通过机械球磨方法进一步制备出高容量镁基复合储氢材料。该材料制备方法克服了镁基储氢合金机械球磨过程中的粘壁现象,提高了材料回收率,且得到了低温吸氢性能优异的高容量镁基复合储氢材料。
The invention relates to a nano-magnesium-based composite hydrogen storage material and a preparation method thereof. The main component of the material is magnesium, and it also contains various catalysts such as mixed rare earth, carbonyl nickel powder and graphite to improve its low-temperature hydrogen absorption performance. The material has a nanocrystalline structure, the grain size is 20-50 nanometers, and has excellent low-temperature hydrogen absorption kinetic properties. In the preparation method, vacuum induction smelting is used to first vacuum smelt pure magnesium and a certain amount of mixed rare earth to prepare a brittle magnesium-rare earth alloy ingot in which magnesium is in-situ doped with rare earth elements; then the obtained alloy is mixed with carbonyl nickel powder, Graphite powder and inert organic grinding aid are mixed, and a high-capacity magnesium-based composite hydrogen storage material is further prepared by mechanical ball milling. The material preparation method overcomes the wall sticking phenomenon during the mechanical ball milling of the magnesium-based hydrogen storage alloy, improves the material recovery rate, and obtains a high-capacity magnesium-based composite hydrogen storage material with excellent low-temperature hydrogen absorption performance.
Description
技术领域technical field
本发明属于储氢材料技术领域,特别涉及一种低温吸氢动力学性能优异的高容量镁基储氢材料及制备方法。The invention belongs to the technical field of hydrogen storage materials, and particularly relates to a high-capacity magnesium-based hydrogen storage material with excellent low-temperature hydrogen absorption kinetic performance and a preparation method.
背景技术Background technique
氢能作为一种清洁高效、储量丰富、可持续的理想二次能源,被视为最具发展潜力的能源材料,得到世界范围内的广泛关注。安全高效的储氢技术是氢能利用过程中的关键环节之一。金属氢化物方法储氢具有体积密度高、可逆性好、安全性高等优点,被认为是最具希望的储氢材料。镁的可逆储氢容量高达7.6wt.%,此外镁还具有资源丰富、价格低廉、环境友好等优点,极具应用前景。尽管镁作为储氢材料满足许多实用条件,但是还不能应用于移动式储氢系统,特别是车载燃料电池供氢装置。这主要是由于纯镁储氢热力学性能差,氢化和脱氢过程需要在300℃以上的条件下进行。此外,纯镁的吸放氢反应速率极为缓慢,无法满足要求。As a clean, efficient, abundant and sustainable ideal secondary energy, hydrogen energy is regarded as an energy material with the most development potential, and has received extensive attention worldwide. Safe and efficient hydrogen storage technology is one of the key links in the process of hydrogen energy utilization. The metal hydride method for hydrogen storage has the advantages of high bulk density, good reversibility, and high safety, and is considered to be the most promising hydrogen storage material. The reversible hydrogen storage capacity of magnesium is as high as 7.6 wt.%. In addition, magnesium has the advantages of abundant resources, low price, and environmental friendliness, and has great application prospects. Although magnesium satisfies many practical conditions as a hydrogen storage material, it cannot be applied to mobile hydrogen storage systems, especially in-vehicle fuel cell hydrogen supply devices. This is mainly due to the poor thermodynamic properties of pure magnesium for hydrogen storage, and the hydrogenation and dehydrogenation processes need to be carried out at temperatures above 300 °C. In addition, the hydrogen absorption and desorption reaction rate of pure magnesium is extremely slow, which cannot meet the requirements.
机械球磨是改善镁基材料储氢性能的有效方法之一,通过球磨方法得到的材料粒径明显减小,表面活性增大。球磨过程中的剪切、研磨和挤压作用使材料内部产生大量缺陷,甚至使得材料的相组成及晶体结构发生改变,从而影响材料的物理和化学性质。专利CN100358624公开了一种在氢气气氛下采用高能球磨制备镁/石墨复合储氢材料的方法,得到的镁基材料晶粒尺寸为70-100nm,虽然很大程度上改善了镁的储氢性能,但反应温度依然很高。专利CN102418018同样公开了一种镁/碳载镍储氢合金粉末制备方法,在100℃下具有较好的吸氢动力学特性。但该材料制备流程极为复杂,生产过程存在困难。Mechanical ball milling is one of the effective methods to improve the hydrogen storage performance of magnesium-based materials. The particle size of the material obtained by the ball milling method is significantly reduced, and the surface activity is increased. The shearing, grinding and squeezing in the ball milling process produce a large number of defects inside the material, and even change the phase composition and crystal structure of the material, thereby affecting the physical and chemical properties of the material. Patent CN100358624 discloses a method for preparing magnesium/graphite composite hydrogen storage material by high-energy ball milling in a hydrogen atmosphere. The obtained magnesium-based material has a grain size of 70-100 nm, although the hydrogen storage performance of magnesium is greatly improved, But the reaction temperature is still high. Patent CN102418018 also discloses a preparation method of magnesium/carbon-supported nickel hydrogen storage alloy powder, which has better hydrogen absorption kinetic characteristics at 100°C. However, the preparation process of this material is extremely complicated, and there are difficulties in the production process.
机械球磨的另一个独特优势就是几乎可以将任何状态的材料进行复合,包括物理性质差别较大的固体与固体、固体与液体以及固体与气体等材料。但是镁具有一定的塑韧性,在机械球磨过程中会粘附在磨球和罐壁上,造成材料成分不均匀。因此,改善镁基合金材料球磨过程中的粘壁现象具有很重要的意义。Another unique advantage of mechanical ball milling is that it can compound materials in almost any state, including solids and solids, solids and liquids, and solids and gases with different physical properties. However, magnesium has a certain plasticity and toughness, and will adhere to the grinding ball and the tank wall during the mechanical ball milling process, resulting in uneven material composition. Therefore, it is of great significance to improve the sticking phenomenon during the ball milling of magnesium-based alloys.
发明内容SUMMARY OF THE INVENTION
本发明的目的是针对当前技术存在的不足,提供一种机械球磨结合多种催化剂协同催化的高容量镁基复合储氢材料及制备方法。该材料以镁为主要吸氢相,包含的催化剂为混合稀土、羰基镍粉和石墨,制备过程辅剂为易挥发的惰性有机溶剂。制备方法为:首先采用真空感应熔炼方法将纯镁与一定量的混合稀土进行真空冶炼,制备出镁原位掺杂稀土元素的脆性镁-稀土合金锭;然后将得到的合金与一定比例的羰基镍粉、石墨粉、惰性有机助磨剂混合,通过机械球磨方法进一步制备出复合材料;最后在真空条件下去除有机液体助磨剂,得到高容量镁基复合储氢材料。通过上述方法成功克服了机械球磨过程中的材料粘壁现象,且可得到多相协同催化的具有纳米晶体结构的镁基复合储氢材料,从而大幅改善了镁基储氢材料的吸氢动力学特性。本发明提供的复合储氢材料可在100℃下快速吸氢,达到实用化需求。The purpose of the present invention is to provide a high-capacity magnesium-based composite hydrogen storage material and a preparation method for the synergistic catalysis of mechanical ball milling and multiple catalysts in view of the deficiencies of the current technology. The material takes magnesium as the main hydrogen-absorbing phase, the catalyst contained is mixed rare earth, carbonyl nickel powder and graphite, and the auxiliary agent in the preparation process is a volatile inert organic solvent. The preparation method is as follows: first, pure magnesium and a certain amount of mixed rare earth are vacuum smelted by a vacuum induction melting method to prepare a brittle magnesium-rare earth alloy ingot in which magnesium is in-situ doped with rare earth elements; then the obtained alloy is mixed with a certain proportion of carbonyl Nickel powder, graphite powder, and inert organic grinding aid are mixed, and the composite material is further prepared by mechanical ball milling; finally, the organic liquid grinding aid is removed under vacuum conditions to obtain a high-capacity magnesium-based composite hydrogen storage material. The above-mentioned method successfully overcomes the material sticking phenomenon in the process of mechanical ball milling, and can obtain a magnesium-based composite hydrogen storage material with a nanocrystalline structure of multiphase synergistic catalysis, thereby greatly improving the hydrogen absorption kinetics of the magnesium-based hydrogen storage material. characteristic. The composite hydrogen storage material provided by the invention can rapidly absorb hydrogen at 100° C. to meet practical requirements.
本发明技术方案如下:The technical scheme of the present invention is as follows:
一种纳米镁基复合储氢材料,该材料主要成分为镁,并由混合稀土、羰基镍粉和石墨多种材料协同催化制得,具有纳米晶体结构,晶粒尺寸为20-50纳米;且具有优异的低温吸氢动力学性能;其中,混合稀土占纯镁质量的10-15%,羰基镍粉占镁-稀土总质量的3-10%,石墨占镁-稀土总质量的3-5%。A nano-magnesium-based composite hydrogen storage material, the main component of which is magnesium, and is prepared by synergistic catalysis of mixed rare earth, carbonyl nickel powder and graphite, and has a nano-crystalline structure and a grain size of 20-50 nanometers; and It has excellent low temperature hydrogen absorption kinetic properties; among them, mixed rare earths account for 10-15% of the mass of pure magnesium, carbonyl nickel powder accounts for 3-10% of the total mass of magnesium-rare earths, and graphite accounts for 3-5% of the total mass of magnesium-rare earths. %.
所述镁基复合储氢材料的优异低温吸氢动力学性能具体为在100℃和3MPa氢压条件下可在30秒内吸收5-6.5wt%的氢。The excellent low-temperature hydrogen absorption kinetic performance of the magnesium-based composite hydrogen storage material is specifically that it can absorb 5-6.5 wt % of hydrogen within 30 seconds under the conditions of 100° C. and 3 MPa hydrogen pressure.
所述的镁基复合储氢材料制备方法,包含以下主要步骤:The preparation method of the magnesium-based composite hydrogen storage material comprises the following main steps:
a、以镁和混合稀土金属为原材料,采用真空感应熔炼方法制备脆性镁-稀土合金锭;其中,熔炼炉背底真空为2.0×10-2Pa,保护气体为0.04-0.06MPa压力的高纯氩气,真空熔炼时的感应线圈功率为8-10kW,熔体保温时间为10-15分钟;熔炼完毕后浇注成铸锭;所述的混合稀土的质量为镁-稀土合金质量分数的10-15%;a. Using magnesium and mixed rare earth metals as raw materials, vacuum induction melting method is used to prepare brittle magnesium-rare earth alloy ingots; wherein, the vacuum at the back of the melting furnace is 2.0×10 -2 Pa, and the protective gas is high-purity high-purity 0.04-0.06MPa pressure. Argon, the induction coil power during vacuum smelting is 8-10kW, and the melt holding time is 10-15 minutes; after the smelting is completed, it is poured into an ingot; the quality of the mixed rare earth is 10-10-10% of the mass fraction of the magnesium-rare earth alloy. 15%;
b、将得到的镁-稀土合金铸锭机械破碎为100目以下的合金粉末,然后与羰基镍粉、石墨粉以及有机液体助磨剂混合均匀,用行星式机械球磨机研磨5-10小时;b. The obtained magnesium-rare earth alloy ingot is mechanically crushed into alloy powder below 100 mesh, then mixed with carbonyl nickel powder, graphite powder and organic liquid grinding aid, and ground with a planetary mechanical ball mill for 5-10 hours;
其中,所述的羰基镍粉的质量为镁-稀土合金粉末质量的3-10%;所述的石墨粉的质量为镁-稀土合金粉末质量的3-5%;所述的有机液体助磨剂的质量为镁-稀土合金粉末质量的50-100%;Wherein, the mass of the carbonyl nickel powder is 3-10% of the mass of the magnesium-rare earth alloy powder; the mass of the graphite powder is 3-5% of the mass of the magnesium-rare earth alloy powder; the organic liquid grinding aid The mass of the agent is 50-100% of the mass of the magnesium-rare earth alloy powder;
c、将球磨后的混合材料在室温下真空干燥,得到镁基复合储氢材料。c. Vacuum-drying the ball-milled mixed material at room temperature to obtain a magnesium-based composite hydrogen storage material.
所述混合稀土包含镧、铈、镨、钕、钐以及其它少量的稀土元素和极少量的杂质元素,稀土元素总含量大于99.5%。The mixed rare earth contains lanthanum, cerium, praseodymium, neodymium, samarium and other small amounts of rare earth elements and a very small amount of impurity elements, and the total content of rare earth elements is greater than 99.5%.
所述的羰基镍粉是指通过还原羰基镍得到的超细镍粉,粒度范围为0.5-1微米。The carbonyl nickel powder refers to ultrafine nickel powder obtained by reducing carbonyl nickel, and the particle size range is 0.5-1 micron.
所述的有机液体助磨剂,可以是乙醇、环己烷、己烷、正庚烷、苯、甲苯、四氢呋喃中的一种或几种。The organic liquid grinding aid can be one or more of ethanol, cyclohexane, hexane, n-heptane, benzene, toluene and tetrahydrofuran.
所述的高纯氩气的纯度为99.999Vol.%。The purity of the high-purity argon is 99.999 Vol.%.
所述的镁基复合储氢材料制备方法,其在机械球磨过程中基本不存在材料的粘壁现象。In the method for preparing the magnesium-based composite hydrogen storage material, there is basically no sticking phenomenon of the material in the process of mechanical ball milling.
本发明的实质性特点为:The essential features of the present invention are:
本发明在高容量镁基储氢材料的制备中使用了混合稀土,不但通过将其与镁冶炼后形成脆性合金,提高球磨效率和克服粘壁现象,更主要的是在吸放氢过程中起到纳米相催化作用,提升了材料的低温吸氢性能。The invention uses mixed rare earths in the preparation of high-capacity magnesium-based hydrogen storage materials, which not only improves the ball milling efficiency and overcomes the wall sticking phenomenon by smelting it with magnesium to form a brittle alloy, but also plays an important role in the process of hydrogen absorption and desorption. The nano-phase catalysis improves the low-temperature hydrogen absorption performance of the material.
本发明的有益效果在于:The beneficial effects of the present invention are:
1)以脆性镁-稀土合金为原材料进行机械球磨,并在球磨过程中添加石墨粉,改善了球磨效率,克服球磨过程中的粘壁效果,使得样品回收率基本高于90%,最高可达99%;2)稀土元素、石墨、羰基镍粉的协同催化作用大幅提升了镁的可逆储氢特性,使得材料在100℃条件下快速吸氢,性能优于现有公开文献资料,在燃料电池汽车用金属氢化物储氢系统方面表现出很好的应用前景。1) Mechanical ball milling is carried out with brittle magnesium-rare earth alloy as raw material, and graphite powder is added in the ball milling process, which improves the ball milling efficiency, overcomes the sticking effect during the ball milling process, and makes the sample recovery rate basically higher than 90%, up to 99%; 2) The synergistic catalysis of rare earth elements, graphite, and carbonyl nickel powder greatly improves the reversible hydrogen storage properties of magnesium, making the material rapidly absorb hydrogen at 100 °C, and its performance is better than the existing published literature. Metal hydride hydrogen storage systems for automobiles have shown good application prospects.
附图说明Description of drawings
图1为本发明所述实施例1得到的储氢材料SEM微观形貌图。FIG. 1 is a SEM microscopic topography diagram of the hydrogen storage material obtained in Example 1 of the present invention.
图2为本发明所述实施例3得到的储氢材料SEM微观形貌图。FIG. 2 is a SEM microscopic topography diagram of the hydrogen storage material obtained in Example 3 of the present invention.
图3为本发明所述实施例4得到的储氢材料吸氢后的TEM微观形貌图。3 is a TEM microscopic topography diagram of the hydrogen storage material obtained in Example 4 of the present invention after hydrogen absorption.
图4为本发明所述实施例5得到的储氢材料SEM微观形貌图。FIG. 4 is a SEM microscopic topography diagram of the hydrogen storage material obtained in Example 5 of the present invention.
图5为本发明所述实施例1得到的储氢材料在不同温度下的吸氢动力学曲线。FIG. 5 is the hydrogen absorption kinetic curve of the hydrogen storage material obtained in Example 1 of the present invention at different temperatures.
图6为本发明所述实施例2得到的储氢材料在不同温度下的吸氢动力学曲线。FIG. 6 is the hydrogen absorption kinetic curve of the hydrogen storage material obtained in Example 2 of the present invention at different temperatures.
图7为本发明所述实施例3得到的储氢材料在不同温度下的吸氢动力学曲线。FIG. 7 is the hydrogen absorption kinetic curve of the hydrogen storage material obtained in Example 3 of the present invention at different temperatures.
图8为本发明所述实施例4得到的储氢材料在不同温度下的吸氢动力学曲线。FIG. 8 is the hydrogen absorption kinetic curve of the hydrogen storage material obtained in Example 4 of the present invention at different temperatures.
图9为本发明所述实施例5得到的储氢材料在不同温度下的吸氢动力学曲线。FIG. 9 is the hydrogen absorption kinetic curve of the hydrogen storage material obtained in Example 5 of the present invention at different temperatures.
具体实施方式Detailed ways
下面结合实施例对本发明进行进一步的详细说明。The present invention will be further described in detail below in conjunction with the examples.
所述的羰基镍粉为公知材料,是指通过还原羰基镍得到的超细镍粉,本发明实施例中使用的羰基镍粉粒度范围为0.5-1微米。The carbonyl nickel powder is a well-known material, and refers to the ultrafine nickel powder obtained by reducing the carbonyl nickel powder. The carbonyl nickel powder used in the embodiment of the present invention has a particle size range of 0.5-1 micron.
所述混合稀土是公知材料,指自然界中的天然稀土矿经提纯、冶炼后得到的稀土金属混合物,包含镧、铈、镨、钕、钐以及其它少量的稀土元素和杂质元素,稀土元素总含量大于99.5%,各个稀土元素比例随产地和批次略有不同,但不影响本发明使用效果;以下实施例涉及的混合稀土金属购自包头稀土研究院(CAS:62379-61-7),但本发明不限于此。The mixed rare earth is a well-known material, which refers to the rare earth metal mixture obtained after purification and smelting of natural rare earth ore in nature, including lanthanum, cerium, praseodymium, neodymium, samarium and other small amounts of rare earth elements and impurity elements, and the total content of rare earth elements. More than 99.5%, the proportion of each rare earth element is slightly different with the place of origin and batch, but it does not affect the use effect of the present invention; the mixed rare earth metals involved in the following examples were purchased from Baotou Rare Earth Research Institute (CAS: 62379-61-7), but The present invention is not limited to this.
实施例1Example 1
将1kg的纯镁锭(纯度大于99%)与0.15kg(15wt%)的混合稀土金属放入真空感应熔炼炉的镁砂坩埚中,抽真空至2.0×10-2Pa以下,然后充入0.04-0.06MPa压力的高纯氩气(纯度为99.999Vol.%)。调整中频感应线圈功率至8-10kW,加热金属原料,待所有金属块完全熔化后,继续保温10-15分钟,使合金成分均匀化。熔炼完毕后在铸铁模具中将合金熔体浇注成直径为30mm的圆形铸锭,冷却至室温后得到镁-稀土合金锭。将合金锭机械粉碎后过100目的标准筛,然后取镁-稀土合金粉末5g、羰基镍粉0.25g(5wt%)、石墨粉0.15g(3wt%)、有机液体助磨剂四氢呋喃5g(100wt%)置于300ml的不锈钢真空球磨罐中,然后放入玛瑙磨球,抽真空后充入0.15MPa的高纯氩气作为保护气体。本发明实施例中采用的球料比为20:1,球磨机转速350r/min,球磨时间10小时。将球磨后的材料置于真空干燥箱中,在室温下真空干燥2小时以上,得到镁基储氢材料。以样品回收率来衡量材料的粘壁程度,即收回固体样品的质量与投入固体原材料质量的百分比。回收率的大小可以反映材料在球磨过程中的粘壁现象,样品回收率越低,表明材料在球磨过程中的粘壁效果越显著,越不利于材料制备。本实施例中材料回收率约为88%。Put 1kg of pure magnesium ingot (purity greater than 99%) and 0.15kg (15wt%) of mixed rare earth metal into the magnesia crucible of vacuum induction melting furnace, evacuate to below 2.0×10 -2 Pa, and then fill with 0.04 -High-purity argon gas at a pressure of 0.06 MPa (purity of 99.999 Vol.%). Adjust the power of the intermediate frequency induction coil to 8-10kW, and heat the metal raw materials. After all the metal blocks are completely melted, continue to keep the temperature for 10-15 minutes to homogenize the alloy composition. After the smelting is completed, the alloy melt is poured into a circular ingot with a diameter of 30 mm in a cast iron mold, and the magnesium-rare earth alloy ingot is obtained after cooling to room temperature. The alloy ingot was mechanically pulverized and passed through a 100-mesh standard sieve, and then 5 g of magnesium-rare earth alloy powder, 0.25 g (5 wt %) of carbonyl nickel powder, 0.15 g (3 wt %) of graphite powder, and 5 g (100 wt %) of organic liquid grinding aid tetrahydrofuran were taken. ) was placed in a 300ml stainless steel vacuum ball mill jar, then put in agate grinding balls, and filled with 0.15MPa high-purity argon as protective gas after vacuuming. The ball-to-material ratio adopted in the embodiment of the present invention is 20:1, the rotational speed of the ball mill is 350 r/min, and the ball milling time is 10 hours. The ball-milled material is placed in a vacuum drying oven, and vacuum-dried at room temperature for more than 2 hours to obtain a magnesium-based hydrogen storage material. The degree of adhesion of the material is measured by the sample recovery rate, that is, the percentage of the mass of the recovered solid sample to the mass of the input solid raw material. The size of the recovery rate can reflect the sticking phenomenon of the material during the ball milling process. The lower the sample recovery rate, the more significant the sticking effect of the material during the ball milling process, and the less conducive to the material preparation. The material recovery rate in this example is about 88%.
用SEM观察了复合材料的微观结构,发现材料是由小颗粒团聚而成的大颗粒组成,大粒径为10-50微米,如附图1所示。添加的羰基镍粉和石墨在机械球磨作用下均匀分散在材料基体内部,形成复合材料。用Sieverts设备在300℃下对材料进行5次活化吸放氢处理,动力学性能稳定后测试了材料的等温吸氢曲线,初始氢压为3MPa,测试温度分别为300、200、100℃,结果如附图5所示。可以看出材料在300℃下经过5分钟后的饱和吸氢量为5.9wt%。降低温度反而大幅提升了材料的吸氢动力学性能,在100℃条件下材料在30秒内的吸氢量可达到5.7wt%,表现出极好的低温吸氢动力学特性。The microstructure of the composite material was observed by SEM, and it was found that the material was composed of large particles formed by agglomeration of small particles, and the large particle size was 10-50 microns, as shown in Figure 1. The added nickel carbonyl powder and graphite are uniformly dispersed inside the material matrix under the action of mechanical ball milling to form a composite material. The material was activated and desorbed for 5 times at 300 °C with Sieverts equipment. After the kinetic properties were stabilized, the isothermal hydrogen absorption curve of the material was tested. The initial hydrogen pressure was 3MPa, and the test temperature was 300, 200, and 100 °C. The results As shown in Figure 5. It can be seen that the saturated hydrogen absorption of the material after 5 minutes at 300°C is 5.9 wt%. Lowering the temperature greatly improves the hydrogen absorption kinetics of the material. At 100 °C, the hydrogen absorption of the material can reach 5.7 wt% within 30 seconds, showing excellent low-temperature hydrogen absorption kinetics.
实施例2Example 2
本实施例中的材料制备方法其它步骤与实施例1相同,不同之处在于球磨时间为5小时,球磨过程中的羰基镍粉为0.5g(10wt%),石墨粉为0.25g(5wt%),助磨剂为乙醇,助磨剂添加量为2.5g(50wt%)。The other steps of the material preparation method in this example are the same as those in Example 1, except that the ball milling time is 5 hours, the carbonyl nickel powder in the ball milling process is 0.5g (10wt%), and the graphite powder is 0.25g (5wt%) , the grinding aid is ethanol, and the added amount of the grinding aid is 2.5g (50wt%).
球磨后的材料未发现明显的粘壁现象,材料回收率约为94%。该复合材料经5次吸放氢活化后的吸氢动力学曲线如附图6所示。可以看出材料在300℃下经过5分钟后的饱和吸氢量约为5.2wt%,略低于实施例1。在100℃下材料同样具有很好的吸氢动力学特性,在30秒内的吸氢量可达到5wt%以上。No obvious sticking phenomenon was found in the ball-milled material, and the material recovery rate was about 94%. The hydrogen absorption kinetic curve of the composite material after 5 times of hydrogen absorption and desorption activation is shown in FIG. 6 . It can be seen that the saturated hydrogen absorption of the material after 5 minutes at 300° C. is about 5.2 wt %, which is slightly lower than that of Example 1. The material also has good hydrogen absorption kinetics at 100 °C, and the hydrogen absorption amount can reach more than 5 wt% within 30 seconds.
实施例3Example 3
本实施例中的材料制备方法其它步骤与实施例1相同,不同之处在于合金熔炼过程中稀土添加量为0.1kg(10wt%),球磨过程中的羰基镍粉质量为0.15g(3wt%),石墨粉质量为0.05g(1wt%),助磨剂为正庚烷。The other steps of the material preparation method in this example are the same as those in Example 1, except that the amount of rare earth added in the alloy smelting process is 0.1kg (10wt%), and the mass of carbonyl nickel powder in the ball milling process is 0.15g (3wt%) , the mass of graphite powder is 0.05g (1wt%), and the grinding aid is n-heptane.
球磨后的材料有较为明显的粘壁现象,样品回收率约为68%。该实施例复合材料SEM微观结构如附图2所示,材料同样由细小颗粒团簇而成,大颗粒粒径为10-70微米。材料经5次吸放氢活化后的吸氢动力学曲线如附图7所示。可以看出材料在300℃下经过5分钟后的饱和吸氢量约为6.3wt%,但是在100℃下材料吸氢动力学性能没有得到明显提升,吸氢速率远低于实施例1和实施例2,这是由于本实施例中石墨粉含量较低,球磨后的材料成分不够均匀,羰基镍粉未能均匀分散在合金内部,其催化作用有限。The material after ball milling has obvious sticking phenomenon, and the sample recovery rate is about 68%. The SEM microstructure of the composite material of this embodiment is shown in FIG. 2 , and the material is also formed by clusters of fine particles, and the size of the large particles is 10-70 μm. The hydrogen absorption kinetic curve of the material after 5 times of hydrogen absorption and desorption activation is shown in Figure 7. It can be seen that the saturated hydrogen absorption of the material after 5 minutes at 300 °C is about 6.3 wt%, but the kinetic performance of hydrogen absorption of the material is not significantly improved at 100 °C, and the hydrogen absorption rate is much lower than that of Example 1 and Example 1. Example 2, this is because the graphite powder content in this example is low, the material composition after ball milling is not uniform enough, the carbonyl nickel powder cannot be uniformly dispersed in the alloy, and its catalytic effect is limited.
实施例4Example 4
本实施例中的材料制备方法其它步骤与实施例1相同,不同之处在于合金熔炼过程中稀土添加量为0.1kg(10wt%),助磨剂为环己烷。The other steps of the material preparation method in this example are the same as those in Example 1, except that the amount of rare earth added during the alloy smelting process is 0.1 kg (10 wt%), and the grinding aid is cyclohexane.
球磨后的材料未发现明显的粘壁现象,材料回收率约为93%。该实施例材料经5次活化吸放氢循环后的TEM微观结构如附图3所示,可以看出材料由20-50纳米的晶粒构成,整体表现为纳米晶结构。材料经5次吸放氢活化后的吸氢动力学曲线如附图8所示。可以看出材料在300℃下经过5分钟后的饱和吸氢量约为6.1wt%。在100℃下该实施例得到的镁基复合材料同样具有优异的吸氢动力学性能,在30秒内的吸氢量可达到6wt%以上。No obvious sticking phenomenon was found in the ball-milled material, and the material recovery rate was about 93%. Figure 3 shows the TEM microstructure of the material of this example after 5 activation cycles of hydrogen absorption and desorption. It can be seen that the material is composed of crystal grains of 20-50 nanometers, and the overall appearance is nanocrystalline structure. The hydrogen absorption kinetic curve of the material after 5 times of hydrogen absorption and desorption activation is shown in Figure 8. It can be seen that the saturated hydrogen absorption of the material after 5 minutes at 300 °C is about 6.1 wt%. At 100°C, the magnesium-based composite material obtained in this example also has excellent hydrogen absorption kinetic properties, and the hydrogen absorption amount within 30 seconds can reach more than 6 wt%.
实施例5Example 5
本实施例中的材料制备方法其它步骤与实施例1相同,不同之处在于合金熔炼过程中稀土添加量为0.1kg(10wt%),石墨粉质量为0.5g(10wt%),助磨剂为环己烷。The other steps of the material preparation method in this example are the same as those in Example 1, except that the amount of rare earth added during the alloy smelting process is 0.1kg (10wt%), the mass of graphite powder is 0.5g (10wt%), and the grinding aid is Cyclohexane.
球磨后的材料完全没有粘壁现象,材料回收率为99%。该实施例复合材料SEM微观结构如附图4所示,可以看出材料由粗大的颗粒构成,石墨粉分布在合金颗粒间。较高的石墨粉含量产生的过度润滑作用导致球磨效率急剧下降,添加的镍几乎没有进入合金内部。该复合材料经5次吸放氢活化后的吸氢动力学曲线如附图9所示。可以看出材料在300℃下经过10分钟后的饱和吸氢量约为5.6wt%。较低的温度下该实施例中的镁基复合材料具有很差的动力学性能,在100℃下经10分钟后的吸氢量也仅为2.8wt%。可见较高的石墨添加量不利于提升材料的吸氢动力学特性。The material after ball milling has no sticking phenomenon at all, and the material recovery rate is 99%. The SEM microstructure of the composite material of this example is shown in FIG. 4 , it can be seen that the material is composed of coarse particles, and the graphite powder is distributed among the alloy particles. The excessive lubrication produced by the higher graphite powder content resulted in a sharp drop in the ball milling efficiency, with little added nickel entering the interior of the alloy. The hydrogen absorption kinetic curve of the composite material after 5 times of hydrogen absorption and desorption activation is shown in FIG. 9 . It can be seen that the saturated hydrogen absorption of the material after 10 minutes at 300 °C is about 5.6 wt%. At lower temperature, the magnesium-based composite material in this example has poor kinetic properties, and the hydrogen absorption after 10 minutes at 100° C. is only 2.8 wt %. It can be seen that a higher amount of graphite is not conducive to improving the hydrogen absorption kinetics of the material.
本发明选取混合稀土元素与镁进行合金熔炼,一方面,镁与稀土元素通过真空感应熔炼后形成金属间化合物,提高了镁基合金的脆性,可以改善材料在球磨过程中的破碎效率和粘壁现象;另一方面,复合材料中的稀土元素在氢化过程中原位析出纳米稀土氢化物二次相,可作为催化剂来改善镁的储氢性能。少量的稀土元素无法使合金形成脆性相,过多的稀土元素会降低材料的可逆储氢容量。经多次实验发现,10-15wt%的混合稀土与镁合金化具有最优的综合性能。石墨的润滑作用既可以改善球磨过程中的粘壁现象,又可以提升羰基镍粉与合金基体的接触效果,促进镍在合金基体中的分散作用,进而提高镍在材料吸放氢反应过程中的催化效率。但过多的石墨在球磨过程中产生过量的润滑作用,例如上述实施例5中石墨含量为10wt%,反而使得球磨效率下降,不利于提升材料的吸氢速率及可逆储氢容量。通过对比上述实施例结果,认为实施例4提供的材料配比具有最优的综合吸氢性能。The invention selects mixed rare earth elements and magnesium for alloy smelting. On the one hand, magnesium and rare earth elements form intermetallic compounds after vacuum induction melting, which improves the brittleness of magnesium-based alloys, and can improve the crushing efficiency and sticking of materials in the ball milling process. phenomenon; on the other hand, the rare earth elements in the composites precipitated nano-rare earth hydride secondary phases in situ during the hydrogenation process, which can be used as catalysts to improve the hydrogen storage performance of magnesium. A small amount of rare earth elements cannot make the alloy form a brittle phase, and too much rare earth elements will reduce the reversible hydrogen storage capacity of the material. After many experiments, it has been found that 10-15wt% of misch metal alloyed with magnesium has the best comprehensive performance. The lubricating effect of graphite can not only improve the sticking phenomenon in the ball milling process, but also improve the contact effect between the carbonyl nickel powder and the alloy matrix, promote the dispersion of nickel in the alloy matrix, and then improve the effect of nickel in the hydrogen absorption and desorption reaction of the material. catalytic efficiency. However, too much graphite produces excessive lubrication in the ball milling process. For example, the graphite content in Example 5 is 10wt%, which reduces the ball milling efficiency, which is not conducive to improving the hydrogen absorption rate and reversible hydrogen storage capacity of the material. By comparing the results of the above examples, it is considered that the material ratio provided in Example 4 has the best comprehensive hydrogen absorption performance.
本发明未尽事宜为公知技术。Matters not addressed in the present invention are known in the art.
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