CN101565168B - Preparation method of multi-light metal coordination aluminum hydride hydrogen storage material - Google Patents
Preparation method of multi-light metal coordination aluminum hydride hydrogen storage material Download PDFInfo
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- CN101565168B CN101565168B CN2009100961845A CN200910096184A CN101565168B CN 101565168 B CN101565168 B CN 101565168B CN 2009100961845 A CN2009100961845 A CN 2009100961845A CN 200910096184 A CN200910096184 A CN 200910096184A CN 101565168 B CN101565168 B CN 101565168B
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Abstract
The invention discloses a preparation method of multi-light metal coordination aluminum hydride hydrogen storage material, NaxLi(3-x)AlH6 (0<=x<=3). The method comprises the following steps of: mixing NaH, LiH and simple substance Al powder, adding a small amount of Ti, Zr, V, Sc or rear earth-based catalysts, and mechanically milling for 60 to140h at the atmosphere of hydrogen so as to synthetize the NaxLi(3-x)AlH6 (0<=x<=3) multi-light metal coordination aluminum hydride. The method has the advantages that: the provided synthetic method is capable of directly synthesizing the final product of NaxLi(3-x)AlH6 (0<=x<=3) at room temperature by ball milling, the operation is simple, the energy consumption is low, the method is safe and reliable; in addition, the synthesized material has high yield, and high reversible hydriding and dehydriding capacity at medium and low temperature, thus being a novel hydrogen storage material with infinite commercial value.
Description
Technical field
The invention belongs to the hydrogen storage material technical field, specifically is a kind of preparation method who directly synthesizes multi-light metal coordination aluminum hydride hydrogen storage material with mechanical ball milling.
Background technology
Face the dual-pressure of the day by day deficient and deterioration of the ecological environment of petroleum resources, utilize this clean energy of Hydrogen Energy to replace the common recognition that has become the whole world based on the existing energy of fossil oil.With hydrogen is that the Proton Exchange Membrane Fuel Cells of fuel and the technical progress and the marketization of electromobile have further promoted hydrogen energy system Study on Technology and development, and in hydrogen energy system technology chain, hydrogen storage technology is considered to the key link.So far, all successful operations on hydrogen-burning automobile or electromobile of the liquid hydrogen in the hydrogen storage technology, lightweight high pressure vessel and metal hydride system.The security of metal hydride is best in above-mentioned three kinds of hydrogen storage systems, the volume hydrogen-storage density is the highest, but the unit weight hydrogen-storage density is very low.For example, only the hydrogen-storage amount with hydrogen storage material itself is an example, and titanium is AB type and AB
2The hydrogen storage capability of type hydrogen storage alloy all is lower than 2.0wt.%, and rare earth is AB
5The type alloy only is 1.4wt.%.
1997, the investigator found, by a small amount of transition-metal catalyst that mixes (especially Ti catalyzer), NaAlH
4Hydrogen discharging temperature drop to 160 ℃ from traditional 250 ℃, and realized reversible hydrogen adsorption and desorption.This technology makes the metal-complexing alanate be expected to develop into a kind of hydrogen storage material of new heavy body, so caused widely and pay close attention to.For the multi-element metal coordination aluminum hydride, early stage, document P. Claudy, B.Bonnetot, J.-P.Bastide, J.-M.Letoffe, Mater.Res.Bull.17 (1982) 1499 reports utilize LiAlH
4In toluene, carry out high pressure, pyroreaction with preparation Na with NaH
2LiAlH
6Technology, but this method needs to filter, cleans, oven dry, just can obtain comparatively purified Na
2LiAlH
6, whole process must be finished under inert gas atmosphere, and is very loaded down with trivial details.Recently, document J.Huot, S.Boily, V.G ü ther, R.Schulz, J.Alloys Compd.383 (1999) 304 utilizes the method for high-energy ball milling, with NaH, LiH and NaAlH
4For raw material has synthesized Na
2LiAlH
6Document A.Fossdal, H.W.Brinks, J.E.
B.C.Hauback, J.Alloys Compd.397 (2005) 135 utilizes the method for high-energy ball milling, with LiH and NaAlH
4For raw material has synthesized Na
2LiAlH
6Though these two kinds of preparation methods have avoided steps such as filtration, cleaning, oven dry, be raw material but still need alanate, and the preparation of alanate itself is just very complicated, cost is also high especially, and therefore, these two kinds of methods also are difficult to large-scale application.
Chinese patent 200810060367.6 discloses the directly synthetic coordination aluminum hydride MNH of employing mechanical ball milling method
4The method of hydrogen storage material has the advantages that raw material is simple, energy consumption is low, cost is low.But the synthetic material is inhaled and to be put the hydrogen process and will could inhale that to put hydrogen complete through two-step reaction.
Summary of the invention
Of the present invention on Chinese patent 200810060367.6 bases, adopt different proportioning raw materials, synthesized the new complex hydrides Na of a class
xLi
3-xAlH
6(0≤x<3) hydrogen storage material, hydrogen is put in the suction of synthetic material only needs single step reaction to finish.
A kind of multi-light metal coordination aluminum hydride hydrogen storage material Na of the present invention
xLi
3-xAlH
6The preparation method, 0≤x in the formula<3 is characterized in that: with NaH, LiH and simple substance Al powder is raw material, it is synthetic at next step ball milling of hydrogen atmosphere to be catalyzer with titanium, zirconium, vanadium, scandium, rare earth, preparation process is as follows:
(1) under the protective atmosphere of room temperature and rare gas element, with the mol ratio of NaH, LiH and simple substance Al powder is NaH: LiH: Al=x: 3-x: 1 mixes, add metal-powder or one or more catalyzer uniform mixing of its halogenide of titaniferous, zirconium, vanadium, scandium, rare earth, the mol ratio of described raw material and catalyzer is 1: 0.01~0.08;
(2) raw material that (1) is obtained and the catalyst mix powder ball grinder that places ball mill, the degassing of sealing final vacuum is to 10
-3Bar;
(3) ball grinder after will outgasing charges into the hydrogen of 1~9MPa, places ball milling 60~140h on the ball mill, just can obtain Na
xLi
3-xAlH
6
Put into ball grinder after mixture of the present invention mixes and put into Wimet abrading-ball about diameter 10mm simultaneously, the weight ratio of abrading-ball and mix powder is 10-100: 1.
When ball milling synthesized, catalyzer can be metal-powder or one or more mixing of its halogenide of titanium, zirconium, vanadium, scandium, rare earth.As the chemosynthesis reaction material that participates in reaction, the height of hydrogen pressure is extremely important.As the hydrogen concentration deficiency that participates in reacting, reacting driving force is little, Na in hydrogenation process
xLi
3-xAlH
6The forming core motivating force of product a little less than, can't directly synthesize Na
xLi
3-xAlH
6, perhaps synthetic Na
xLi
3-xAlH
6Productive rate very low.Be higher than 9MPa when reacting hydrogen pressure, building-up process will under high pressure be carried out, and production cost improves, and processing safety reduces.The present invention is controlled at hydrogen pressure P: 1MPa<P<9MPa.Take all factors into consideration the productive rate and the energy consumption of multi-light metal alanate, the present invention is set in t with ball milling time t and is: 60h<t<140h.
Compared with prior art, beneficial effect of the present invention is:
1) with solvent in the high-temperature high-pressure chemical reaction synthesis process relatively, synthetic method of the present invention can at room temperature be carried out, need not high temperature and a large amount of organic solvents participate in, also needn't carry out such as subsequent disposal such as filtration, cleaning and oven dry, simple to operate, production efficiency is high, energy consumption is low;
2) with utilize NaH, LiH, NaAlH
4Deng being the synthetic Na of raw material
xLi
3-xAlH
6Compare, raw materials used simple, have the advantage that energy consumption is low, cost is low.
3) with the doped catalyst ball milling after carry out hydrogenation again the synthetic complex hydrides of two step method relatively, the present invention is as long as the mechanical ball milling operation can synthesize Na once the step
xLi
3-xAlH
6Productive rate is at the multi-light metal coordination aluminum hydride final product more than 90%.As seen, Production Flow Chart of the present invention is simpler, and production efficiency is higher, and cost is lower, and energy consumption still less is particularly useful for specialized scale operation.
Description of drawings
Fig. 1 mixes Ti catalyst spheres mill synthetic Na
1.8Li
1.2AlH
6The curve of hydrogen desorption kinetics first of complex hydrides;
Fig. 2 mixes TiF
3The catalyst spheres break-in becomes Na
2LiAlH
6XRD figure spectrum before and after the complex hydrides;
Fig. 3 mixes V catalyst spheres mill synthetic Na
2.4Li
0.6AlH
4The curve of hydrogen desorption kinetics first of complex hydrides and preceding 10 round-robin thereof are put the hydrogen capacity contrast.
Embodiment
Embodiment 1
According to chemical formula is Na
xLi
3-xAlH
6Coordinate hydride hydrogen-storing material, x=1.8 promptly constitute Na
1.8Li
1.2AlH
6Complex hydrides.With NaH, LiH and Al powder is raw material, and simple substance Ti powder is a catalyzer, presses NaH: LiH: Al=1.8: 1.2: 1 (mol ratio) calculates the weight proportion of LiH, NaH and Al powder, calculates the doping of Ti powder again by the 4mol.% of (NaH+LiH+Al) integral molar quantity.Above-mentioned NaH purity 〉=95%, particle diameter are 74 μ m; LiH purity 〉=97%, particle diameter are 74 μ m; Al powder purity 〉=99%, particle diameter are 74~154 μ m; Ti powder purity 〉=99%, particle diameter<74 μ m.Raw material packed in the ball grinder with catalyzer and add abrading-ball by 40: 1 ratio of grinding media to material.Earlier ball grinder is found time to be vented to vacuum tightness 10 before the ball milling
-3Bar charges into 3.5MPa purity again greater than 99.9% hydrogen, then ball milling 120h at room temperature.Prepared Na
1.8Li
1.2AlH
6It is 3.10wt.% that hydrogen capacity is put in actual measurement when putting hydrogen first.
The main chemical reactions that reaction process comprises is:
Prepared complex hydrides all adopts " constant volume-pressure differential method " to measure its hydrogen storage property.Suction subsequently, put the hydrogen cycling condition and be: under 100 ℃ and 5MPa, inhale hydrogen, transfer hydrogen (down with) at 170~220 ℃ and 0.1MPa.
Fig. 1 is for mixing the synthetic Na of Ti catalyzer institute
1.8Li
1.2AlH
6The curve of hydrogen desorption kinetics first of complex hydrides.Prepared material is transferred hydrogen can reach 3.10wt.% in the time of 4.5 hours the hydrogen capacity of putting at 200 ℃.
Embodiment 2
According to chemical formula is Na
xLi
3-xAlH
6Coordinate hydride hydrogen-storing material, x=2 promptly constitutes Na
2LiAlH
6Complex hydrides.With NaH, LiH and Al powder is raw material, TiF
3Be catalyzer, press NaH: LiH: Al=2: 1: 1 (mol ratio) calculates the weight proportion of NaH, LiH and Al powder, and the 2mol.% by (NaH+LiH+Al) integral molar quantity calculates TiF again
3Doping.Above-mentioned NaH purity 〉=95%, particle diameter are 74 μ m; LiH purity 〉=97%, particle diameter are 74 μ m; Al powder purity 〉=99%, particle diameter are 74~154 μ m; TiF
3Powder purity 〉=99%, particle diameter≤154 μ m.Raw material packed in the ball grinder with catalyzer and add abrading-ball by 30: 1 ratio of grinding media to material.Earlier ball grinder is found time to be vented to vacuum tightness 10 before the ball milling
-3Bar charges into purity 〉=99.9%, 2.5MPa hydrogen again, then ball milling 100h at room temperature, the so Na of preparation
2LiAlH
6The hydrogen storage capability actual measurement is 3.14wt.%.
Fig. 2 is for mixing TiF
3The catalyst spheres break-in becomes Na
2LiAlH
6XRD figure spectrum before and after the complex hydrides.Na in the ball milling synthetic materials
2LiAlH
6Complex hydrides content is up to more than 90%.
Embodiment 3
According to chemical formula is Na
xLi
3-xAlH
6Coordinate hydride hydrogen-storing material, x=2.4 promptly constitutes Na
2.4Li
0.6AlH
6Complex hydrides.With NaH, LiH and Al powder is raw material.Selecting simple substance V powder is catalyzer.Press earlier NaH: LiH: Al=2.4: 0.6: 1 (mol ratio) calculates the weight proportion of NaH, LiH and Al powder, calculates the doping of V catalyzer again by the 4mol.% of (NaH+LiH+Al) integral molar quantity, and V powder median size is about 50 μ m, purity>99%.Raw material parameters such as the purity of NaH, LiH and Al, particle diameter are with embodiment 1.Earlier ball grinder is found time to be vented to vacuum tightness 10 before the ball milling
-3Bar charges into 3.8MPa purity again greater than 99.99% hydrogen, ball milling 130h at room temperature then, the Na for preparing
2.4Li
0.6AlH
6The actual measurement hydrogen storage capability of complex hydrides is 3.03wt.%.
The main chemical reactions that reaction process comprises is:
Fig. 3 is for mixing V catalyst spheres mill synthetic Na
2.4Li
0.6AlH
6The curve of hydrogen desorption kinetics first of complex hydrides and preceding 10 round-robin thereof are put the hydrogen capacity contrast.Prepared Na
2.4Li
0.6AlH
6Can reach the hydrogen capacity of putting of 3.03wt.% when material is put hydrogen first under 190 ℃ in 4 hours, its hydrogen capacity of putting in the hydrogen circulation in 10 suctions subsequently of putting all remains on more than the 2.68wt.%.
Claims (2)
1. multi-light metal coordination aluminum hydride hydrogen storage material Na
xLi
3-xAlH
6The preparation method, 0≤x in the formula<3 is characterized in that: with NaH, LiH and simple substance Al powder is raw material, it is synthetic at next step ball milling of hydrogen atmosphere to be catalyzer with titanium, zirconium, vanadium, scandium, rare earth, preparation process is as follows:
(1) under the protective atmosphere of room temperature and rare gas element, with the mol ratio of NaH, LiH and simple substance Al powder is NaH: LiH: Al=x: 3-x: 1 mixes, add metal-powder or one or more catalyzer uniform mixing of its halogenide of titaniferous, zirconium, vanadium, scandium, rare earth, the mol ratio of described raw material and catalyzer is 1: 0.01~0.08;
(2) raw material that (1) is obtained and the catalyst mix powder ball grinder that places ball mill, the degassing of sealing final vacuum is to 10
-3Bar;
(3) ball grinder after will outgasing charges into the hydrogen of 1~9MPa, places ball milling 60~140h on the ball mill, just can obtain Na
xLi
3-xAlH
6
2. the described multi-light metal coordination aluminum hydride hydrogen storage material Na of root a tree name claim 1
xLi
3-xAlH
6The preparation method, it is characterized in that putting into after mixture mixes ball grinder and put into Wimet abrading-ball about diameter 10mm simultaneously, the weight ratio of abrading-ball and mix powder is 10-100: 1.
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CN102502488B (en) * | 2011-10-26 | 2013-09-04 | 安徽工业大学 | Method for improving hydrogen storage property of lithium borohydride |
CN103407964B (en) * | 2013-08-02 | 2015-04-15 | 浙江大学 | Method for preparing metal coordination hydride nanorods |
AU2016239913B2 (en) * | 2015-04-02 | 2020-08-27 | Albemarle Germany Gmbh | Highly reactive metal hydrides, process for their preparation and use |
CN105645351A (en) * | 2015-12-24 | 2016-06-08 | 浙江大学 | Aluminum hydride hydrogen storage material and preparation method thereof |
CN111498799A (en) * | 2020-06-09 | 2020-08-07 | 世能氢电科技有限公司 | Metal alanate composite hydrogen storage material and preparation method thereof |
CN111704156B (en) * | 2020-07-06 | 2022-07-15 | 宁夏大学 | Transition metal alanate and preparation method thereof |
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