CN107930697A - A kind of 67 composite materials of Pt/ZIF for being used to be catalyzed ammonia borane hydrolysis hydrogen manufacturing - Google Patents
A kind of 67 composite materials of Pt/ZIF for being used to be catalyzed ammonia borane hydrolysis hydrogen manufacturing Download PDFInfo
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- 229910052739 hydrogen Inorganic materials 0.000 title claims abstract description 30
- 239000001257 hydrogen Substances 0.000 title claims abstract description 30
- 239000002131 composite material Substances 0.000 title claims abstract description 23
- 230000007062 hydrolysis Effects 0.000 title claims abstract description 23
- 238000006460 hydrolysis reaction Methods 0.000 title claims abstract description 23
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 title claims abstract description 22
- JBANFLSTOJPTFW-UHFFFAOYSA-N azane;boron Chemical compound [B].N JBANFLSTOJPTFW-UHFFFAOYSA-N 0.000 title claims abstract description 22
- 238000004519 manufacturing process Methods 0.000 title claims description 8
- 239000002105 nanoparticle Substances 0.000 claims abstract description 17
- 239000012621 metal-organic framework Substances 0.000 claims abstract description 15
- 230000004913 activation Effects 0.000 claims abstract description 12
- 238000002360 preparation method Methods 0.000 claims abstract description 11
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 11
- 239000002253 acid Substances 0.000 claims abstract description 10
- 239000007864 aqueous solution Substances 0.000 claims abstract description 8
- 238000006243 chemical reaction Methods 0.000 claims abstract description 8
- 150000002431 hydrogen Chemical class 0.000 claims abstract description 8
- 238000000034 method Methods 0.000 claims abstract description 6
- 238000011068 loading method Methods 0.000 claims abstract description 5
- 229910052751 metal Inorganic materials 0.000 claims abstract description 5
- 239000002184 metal Substances 0.000 claims abstract description 5
- 238000009826 distribution Methods 0.000 claims abstract description 4
- 230000007306 turnover Effects 0.000 claims abstract 4
- 238000001132 ultrasonic dispersion Methods 0.000 claims abstract 2
- 238000003756 stirring Methods 0.000 claims description 10
- 239000000243 solution Substances 0.000 claims description 5
- LXBGSDVWAMZHDD-UHFFFAOYSA-N 2-methyl-1h-imidazole Chemical compound CC1=NC=CN1 LXBGSDVWAMZHDD-UHFFFAOYSA-N 0.000 claims description 4
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 claims description 4
- 239000008367 deionised water Substances 0.000 claims description 4
- 229910021641 deionized water Inorganic materials 0.000 claims description 4
- ZBYYWKJVSFHYJL-UHFFFAOYSA-L cobalt(2+);diacetate;tetrahydrate Chemical compound O.O.O.O.[Co+2].CC([O-])=O.CC([O-])=O ZBYYWKJVSFHYJL-UHFFFAOYSA-L 0.000 claims description 3
- 239000005457 ice water Substances 0.000 claims description 3
- 238000006356 dehydrogenation reaction Methods 0.000 claims description 2
- 238000001514 detection method Methods 0.000 claims description 2
- 239000000203 mixture Substances 0.000 claims description 2
- 238000001035 drying Methods 0.000 claims 2
- 238000001291 vacuum drying Methods 0.000 claims 1
- 230000003197 catalytic effect Effects 0.000 abstract description 12
- 238000002156 mixing Methods 0.000 abstract description 3
- 230000002195 synergetic effect Effects 0.000 abstract description 3
- 230000009467 reduction Effects 0.000 abstract description 2
- 239000002082 metal nanoparticle Substances 0.000 description 13
- 239000003054 catalyst Substances 0.000 description 6
- 229910000510 noble metal Inorganic materials 0.000 description 6
- 238000005054 agglomeration Methods 0.000 description 5
- 230000002776 aggregation Effects 0.000 description 5
- 239000000463 material Substances 0.000 description 4
- 239000000126 substance Substances 0.000 description 4
- 239000011148 porous material Substances 0.000 description 3
- 238000002441 X-ray diffraction Methods 0.000 description 2
- 230000008901 benefit Effects 0.000 description 2
- 230000005540 biological transmission Effects 0.000 description 2
- 238000003795 desorption Methods 0.000 description 2
- 238000010438 heat treatment Methods 0.000 description 2
- 239000003446 ligand Substances 0.000 description 2
- 239000002245 particle Substances 0.000 description 2
- 238000001179 sorption measurement Methods 0.000 description 2
- 239000011232 storage material Substances 0.000 description 2
- 239000000758 substrate Substances 0.000 description 2
- 239000013177 MIL-101 Substances 0.000 description 1
- 239000000956 alloy Substances 0.000 description 1
- 229910045601 alloy Inorganic materials 0.000 description 1
- 239000003575 carbonaceous material Substances 0.000 description 1
- 239000013078 crystal Substances 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 239000006185 dispersion Substances 0.000 description 1
- 125000000524 functional group Chemical group 0.000 description 1
- 230000003993 interaction Effects 0.000 description 1
- 238000001000 micrograph Methods 0.000 description 1
- 231100000252 nontoxic Toxicity 0.000 description 1
- 230000003000 nontoxic effect Effects 0.000 description 1
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- 238000001144 powder X-ray diffraction data Methods 0.000 description 1
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- 230000035484 reaction time Effects 0.000 description 1
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- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J31/00—Catalysts comprising hydrides, coordination complexes or organic compounds
- B01J31/16—Catalysts comprising hydrides, coordination complexes or organic compounds containing coordination complexes
- B01J31/1691—Coordination polymers, e.g. metal-organic frameworks [MOF]
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- C01B3/00—Hydrogen; Gaseous mixtures containing hydrogen; Separation of hydrogen from mixtures containing it; Purification of hydrogen
- C01B3/02—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen
- C01B3/06—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of inorganic compounds containing electro-positively bound hydrogen, e.g. water, acids, bases, ammonia, with inorganic reducing agents
- C01B3/065—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of inorganic compounds containing electro-positively bound hydrogen, e.g. water, acids, bases, ammonia, with inorganic reducing agents from a hydride
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Abstract
本发明公开了一种用于催化氨硼烷水解制氢的Pt/ZIF‑67复合材料,由氯铂酸和金属有机框架ZIF‑67混合后,通过一步还原法制备而成。其结构保留了ZIF‑67框架结构,Pt纳米粒子的平均尺寸为1‑2 nm,且分布均匀,经XRD检测无明显的Pt金属衍射特征峰。其制备方法包括:步骤1)ZIF‑67的制备与活化;步骤2)Pt纳米粒子的负载,将活化后的ZIF‑67加入到水中超声分散,然后加入氯铂酸,再滴加NaBH4水溶液,然后将产物过滤、洗涤后、干燥即可。作为催化氨硼烷水解制氢的应用,反应速率的转化频率值(Turn over frequency,TOF)达到70‑100 mol H2 min‑1 Pt mol‑1,活化能为30‑40 kJ mol‑1。ZIF‑67和Pt纳米粒子的协同作用,带来更好的催化性能,因此,本发明在氢气制备领域具有广阔的应用前景。
The invention discloses a Pt/ZIF-67 composite material for catalyzing the hydrolysis of ammonia borane to produce hydrogen, which is prepared by a one-step reduction method after mixing chloroplatinic acid and metal organic framework ZIF-67. Its structure retains the ZIF-67 framework structure, the average size of Pt nanoparticles is 1-2 nm, and the distribution is uniform, and there is no obvious Pt metal diffraction characteristic peak detected by XRD. The preparation method includes: step 1) preparation and activation of ZIF-67; step 2) loading of Pt nanoparticles, adding activated ZIF-67 to water for ultrasonic dispersion, then adding chloroplatinic acid, and then adding dropwise NaBH 4 aqueous solution , and then the product is filtered, washed and dried. As an application to catalyze the hydrolysis of ammonia borane to produce hydrogen, the reaction rate has a turn over frequency (Turn over frequency, TOF) value of 70‑100 mol H 2 min ‑1 Pt mol ‑1 , and an activation energy of 30‑40 kJ mol ‑1 . The synergistic effect of ZIF-67 and Pt nanoparticles brings better catalytic performance, therefore, the invention has broad application prospects in the field of hydrogen preparation.
Description
技术领域technical field
本发明属于能源技术领域,具体是一种用于催化氨硼烷水解制氢的Pt/ZIF-67复合材料。The invention belongs to the field of energy technology, in particular to a Pt/ZIF-67 composite material used to catalyze the hydrolysis of ammonia borane to produce hydrogen.
背景技术Background technique
在各种化学储氢材料中,氨硼烷(ammonia borane, NH3BH3, AB)具有高达19.6wt%的储氢量,在固态和溶液中具有高稳定性,无毒,溶解性好。因此,它被认为是各种应用中有希望的化学储氢材料之一。储存在氨硼烷中的氢可以利用合适的催化剂通过水解释放出来。迄今为止,已经有各种各样用于催化氨硼烷水解的催化剂,其中贵金属催化剂在水解制氢时表现出快的放氢速率和低的活化能,拥有优异的催化性能。然而,较高的价格限制了其在实际中的生产和应用。为了降低成本,许多研究人员趋向于将贵金属纳米粒子负载在不同的基底(如碳材料,聚合物,金属有机框架)上,不仅可以利用贵金属的高催化活性,而且可以抑制纳米粒子的团聚,进一步提高催化性能。金属有机骨架(Metal organicframeworks, MOFs)也因其独特的高比表面积和孔洞特性以及良好的化学稳定性而备受关注。与其他基底相比,MOFs可以在其框架内控制贵金属纳米粒子的成核和生长,从而防止其团聚。此外,高比表面积和可调孔尺寸的孔洞可以较好地分散贵金属纳米粒子。研究人员发现,将贵金属纳米粒子分散在MOF表面或嵌入MOFs孔中均能提高AB水解的放氢性能。Cai等合成了Ru/MIL-96 催化剂并用于氨硼烷的催化水解,其活化能Ea较高为47.7 kJ mol-1[Int. J. Hydrogen Energy, 2014, 39, 17129-17135]。Luo等将超细的Pd 纳米粒子固定在MIL-101框架中,并测试了其催化氨硼烷水解的性能,但TOF较低,为45 mol H2 min-1 Pdmol-1 [Int. J. Hydrogen Energy, 2014, 39, 4947-4953]。Wang等将AgPd 合金粒子(5-9nm)负载在UIO-66-NH2上,作为氨硼烷水解制氢的催化剂表现出良好的性能,但主要存在金属纳米粒子团聚的问题[Int. J. Hydrogen Energy, 2016, 41, 944-950]。Among various chemical hydrogen storage materials, ammonia borane (NH 3 BH 3 , AB) has a hydrogen storage capacity as high as 19.6wt%, has high stability in solid state and solution, is non-toxic, and has good solubility. Therefore, it is considered as one of the promising chemical hydrogen storage materials in various applications. The hydrogen stored in ammonia borane can be released by hydrolysis using a suitable catalyst. So far, there have been a variety of catalysts used to catalyze the hydrolysis of ammonia borane, among which noble metal catalysts exhibit fast hydrogen desorption rate and low activation energy during hydrolysis to hydrogen production, and have excellent catalytic performance. However, the high price limits its production and application in practice. In order to reduce the cost, many researchers tend to support noble metal nanoparticles on different substrates (such as carbon materials, polymers, metal organic frameworks), which can not only take advantage of the high catalytic activity of noble metals, but also inhibit the agglomeration of nanoparticles, further Improve catalytic performance. Metal organic frameworks (MOFs) have also attracted much attention due to their unique high specific surface area and porosity properties as well as good chemical stability. Compared with other substrates, MOFs can control the nucleation and growth of noble metal nanoparticles within their framework, thereby preventing their agglomeration. In addition, the pores with high specific surface area and tunable pore size can better disperse noble metal nanoparticles. The researchers found that dispersing noble metal nanoparticles on the surface of MOFs or embedding them in the pores of MOFs can enhance the hydrogen release performance of AB hydrolysis. Cai et al. synthesized Ru/MIL-96 catalyst and used it for the catalytic hydrolysis of ammonia borane, and its activation energy E a was as high as 47.7 kJ mol -1 [Int. J. Hydrogen Energy, 2014, 39, 17129-17135]. Luo et al. immobilized ultrafine Pd nanoparticles in the MIL-101 framework and tested its catalytic performance for the hydrolysis of ammonia borane, but the TOF was low at 45 mol H 2 min -1 Pdmol -1 [Int. J. Hydrogen Energy, 2014, 39, 4947-4953]. Wang et al. supported AgPd alloy particles (5-9nm) on UIO-66-NH 2 , which showed good performance as a catalyst for hydrogen production from ammonia borane hydrolysis, but there was mainly the problem of metal nanoparticles agglomeration [Int. J. Hydrogen Energy, 2016, 41, 944-950].
金属纳米粒子的催化性质与其周围的化学环境密切相关,鉴于MOF结构的高度可调控特性,具有不同官能团的配体与金属纳米粒子具有不同的相互作用,因此金属粒子的催化活性也不同。因此,选择适当的配体及MOF材料,才能实现MOF材料与金属纳米粒子之间的协同作用,带来更好的催化性能,是解决上述技术问题的有效途径。The catalytic properties of metal nanoparticles are closely related to their surrounding chemical environment. Given the highly tunable nature of the MOF structure, ligands with different functional groups have different interactions with metal nanoparticles, so the catalytic activity of metal nanoparticles is also different. Therefore, selecting appropriate ligands and MOF materials can realize the synergistic effect between MOF materials and metal nanoparticles and bring about better catalytic performance, which is an effective way to solve the above technical problems.
发明内容Contents of the invention
本发明的目的是提供一种用于催化氨硼烷水解制氢的Pt/ZIF-67复合材料,解决现有技术金属纳米粒子团聚以及TOF值较低,活化能较高的问题。通过使用ZIF-67与Pt进行复合,可以提供更高的比表面积和吸附能力,使金属纳米粒子更加均匀地分散在MOF材料表面;同时,利用ZIF-67实现与Pt纳米粒子之间的协同作用,提高催化性能。The purpose of the present invention is to provide a Pt/ZIF-67 composite material for catalyzing the hydrolysis of ammonia borane to produce hydrogen, which solves the problems of metal nanoparticle agglomeration, low TOF value and high activation energy in the prior art. By using ZIF-67 to combine with Pt, it can provide higher specific surface area and adsorption capacity, so that metal nanoparticles can be more uniformly dispersed on the surface of MOF materials; at the same time, ZIF-67 can be used to achieve synergy with Pt nanoparticles , improve catalytic performance.
为了实现上述发明目的,本发明采用的技术方案包括:In order to realize the foregoing invention object, the technical scheme that the present invention adopts comprises:
Pt/ZIF-67复合材料由氯铂酸和金属有机框架ZIF-67混合后,通过一步还原法制备而成,其结构保留了ZIF-67框架结构。Pt纳米粒子的平均尺寸为1-2 nm,且分布均匀,经XRD检测无明显的Pt金属衍射特征峰。The Pt/ZIF-67 composite was prepared by a one-step reduction method after mixing chloroplatinic acid and metal-organic framework ZIF-67, and its structure retained the ZIF-67 framework structure. The average size of Pt nanoparticles is 1-2 nm, and the distribution is uniform, and there is no obvious Pt metal diffraction characteristic peak through XRD detection.
Pt/ZIF-67复合材料的制备方法,包括以下步骤:The preparation method of Pt/ZIF-67 composite material, comprises the following steps:
步骤1)ZIF-67的制备与活化,将乙酸钴四水合物和2-甲基咪唑加入到水中,超声混合均匀后,随后装入高压反应釜,放入烘箱,恒温加热引发反应,待反应体系缓慢冷却至室温后,将产物取出、洗涤、干燥后得到ZIF-67,并将所得的ZIF-67进行活化,得到活化后的ZIF-67;Step 1) Preparation and activation of ZIF-67, adding cobalt acetate tetrahydrate and 2-methylimidazole into water, ultrasonically mixing evenly, then putting them into a high-pressure reactor, putting them in an oven, heating at a constant temperature to initiate the reaction, and waiting for the reaction After the system is slowly cooled to room temperature, the product is taken out, washed and dried to obtain ZIF-67, and the obtained ZIF-67 is activated to obtain activated ZIF-67;
步骤2)Pt纳米粒子的负载,将活化后的ZIF-67加入到水中,超声分散30-60 min,得到ZIF-67水溶液,然后以活化后的ZIF-67和氯铂酸的质量比满足(5-15):100,将氯铂酸加入ZIF-67水溶液中,室温下搅拌6-24 h,然后在冰水浴下,再将浓度为0.01-0.05 mol/L的NaBH4水溶液边搅拌边滴加到溶液中,继续搅拌1-6 h后,静置,然后将产物过滤,用无水乙醇和去离子水反复多次洗涤后,在60-100 oC下真空干燥10-20 h,得到Pt/ZIF-67复合材料。Step 2) Loading of Pt nanoparticles, adding activated ZIF-67 into water, ultrasonically dispersing for 30-60 min to obtain ZIF-67 aqueous solution, and then satisfying the mass ratio of activated ZIF-67 and chloroplatinic acid ( 5-15): 100, add chloroplatinic acid into the ZIF-67 aqueous solution, stir at room temperature for 6-24 h, and then drop the NaBH 4 aqueous solution with a concentration of 0.01-0.05 mol/L in an ice-water bath while stirring Add it into the solution, continue to stir for 1-6 h, let it stand, then filter the product, wash it repeatedly with absolute ethanol and deionized water, and dry it in vacuum at 60-100 o C for 10-20 h to obtain Pt/ZIF-67 composite.
本发明所述的Pt/ZIF-67复合材料用于催化氨硼烷水解放氢,明显提升了放氢性能,较高的TOF值,为70-100 mol H2 min-1 Pt mol-1,以及较低的活化能,为30-40 kJ mol-1。The Pt/ZIF-67 composite material of the present invention is used to catalyze the hydrolysis of ammonia borane to decompose hydrogen, which significantly improves the dehydrogenation performance, and has a higher TOF value of 70-100 mol H 2 min -1 Pt mol -1 , and a lower activation energy of 30-40 kJ mol -1 .
本发明相对于现有技术,具有以下优点:Compared with the prior art, the present invention has the following advantages:
1. 平均尺寸为1-2 nm 的Pt纳米粒子均匀分布在金属有机框架ZIF-67的表面,有效地抑制了纳米粒子的团聚现象;1. The Pt nanoparticles with an average size of 1-2 nm are uniformly distributed on the surface of metal organic framework ZIF-67, which effectively inhibits the agglomeration of nanoparticles;
2. Pt/ZIF-67复合材料用于催化氨硼烷水解放氢,表现出较好的催化性能,具体表现为较高的TOF值,为70-100 mol H2 min-1 Pt mol-1,以及较低的活化能,为30-40 kJ mol-1。2. The Pt/ZIF-67 composite material is used to catalyze the hydrolysis of ammonia borane to decompose hydrogen, showing good catalytic performance, specifically showing a high TOF value of 70-100 mol H 2 min -1 Pt mol -1 , and a lower activation energy of 30-40 kJ mol -1 .
3. 相对于UIO-66-NH2来说,ZIF-67可以提供更高的比表面积以及较好的吸附能力,可以使金属纳米粒子更好地分散在MOF的表面,更为重要的是,发挥了ZIF-67和Pt纳米粒子的协同作用,带来更好的催化性能;3. Compared with UIO-66-NH 2 , ZIF-67 can provide higher specific surface area and better adsorption capacity, which can better disperse metal nanoparticles on the surface of MOF. More importantly, Played the synergistic effect of ZIF-67 and Pt nanoparticles, resulting in better catalytic performance;
4. 本发明的制氢材料成本低廉,环境友好,工艺简单,适合大批量的制备。4. The hydrogen production material of the present invention is low in cost, environmentally friendly, simple in process, and suitable for mass production.
因此,本发明在氢气制备领域具有广阔的应用前景。Therefore, the present invention has broad application prospects in the field of hydrogen production.
附图说明:Description of drawings:
图1为具体实施例的X射线衍射图;Fig. 1 is the X-ray diffraction figure of specific embodiment;
图2为具体实施例的透射电镜图Fig. 2 is the transmission electron microscope figure of specific embodiment
图3为具体实施例的Pt纳米粒子的粒径分布图;Fig. 3 is the particle size distribution figure of the Pt nanoparticle of specific embodiment;
图4为具体实施例在不同温度下催化氨硼烷水解的放氢速率图;Fig. 4 is the hydrogen release rate figure of specific embodiment catalyzing the hydrolysis of ammonia borane at different temperatures;
图5为具体实施例的阿伦尼乌斯曲线。Fig. 5 is an Arrhenius curve of a specific embodiment.
具体实施方式Detailed ways
本发明通过实施例,结合说明书附图对本发明内容作进一步详细说明,但不是对本发明的限制。The present invention will be described in further detail through the embodiments in conjunction with the accompanying drawings, but it is not intended to limit the present invention.
实施例Example
用于催化氨硼烷水解制氢的Pt/ZIF-67复合材料的具体操作步骤如下:The specific operation steps of the Pt/ZIF-67 composite material used to catalyze the hydrolysis of ammonia borane to produce hydrogen are as follows:
步骤1)ZIF-67的制备与活化,将1 mmol乙酸钴四水合物和20 mmol 2-甲基咪唑加入到20 mL水中,超声混合均匀后,随后装入高压反应釜,放入烘箱,恒温加热到120 oC引发反应,反应时间为18 h,待反应体系缓慢冷却至室温后,将产物取出,用无水乙醇和去离子水反复多次洗涤,在80 oC下干燥后得到ZIF-67,并将所得的ZIF-67在真空条件下,在150 oC下,保温12 h进行活化,得到活化后的ZIF-67;Step 1) Preparation and activation of ZIF-67, add 1 mmol of cobalt acetate tetrahydrate and 20 mmol of 2-methylimidazole into 20 mL of water, mix well by ultrasonic, then put into autoclave, put into oven, keep constant temperature The reaction was initiated by heating to 120 o C, and the reaction time was 18 h. After the reaction system was slowly cooled to room temperature, the product was taken out, washed repeatedly with absolute ethanol and deionized water, and dried at 80 o C to obtain ZIF- 67, and the obtained ZIF-67 was activated under vacuum conditions at 150 o C for 12 h to obtain activated ZIF-67;
步骤2)Pt纳米粒子的负载,将100 mg活化后的ZIF-67加入到15 mL水中,超声分散40min,然后将5 mg氯铂酸加入溶液中,室温下搅拌18 h,然后在冰水浴下,将10mL 0.02 mol/L的NaBH4边搅拌边滴加到溶液中,继续搅拌4 h后,静置,然后将产物过滤,用无水乙醇和去离子水反复多次洗涤后,在80 oC下真空干燥12 h,得到Pt/ZIF-67复合材料。Step 2) Loading of Pt nanoparticles, 100 mg of activated ZIF-67 was added to 15 mL of water, ultrasonically dispersed for 40 min, then 5 mg of chloroplatinic acid was added to the solution, stirred at room temperature for 18 h, and then placed in an ice-water bath , add 10mL of 0.02 mol/L NaBH 4 dropwise into the solution while stirring, continue to stir for 4 h, then let it stand, then filter the product, wash it repeatedly with absolute ethanol and deionized water, and put it at 80 o C under vacuum for 12 h to obtain the Pt/ZIF-67 composite.
测试结果如下:The test results are as follows:
如图1为本发明所制备的ZIF-67以及Pt/ZIF-67复合材料的XRD谱图。在2θ=7.4˚,12.7˚,16.5˚处的特征峰对应的是ZIF-67晶面(011),(112),(013),表明在催化剂制备过程中较好地保留了ZIF-67框架结构。此外,从Pt/ZIF-67的PXRD图谱中没有发现明显的Pt金属衍射特征峰,可能是由于金属纳米颗粒良好的分散性和较低的金属负载量。Figure 1 shows the XRD spectra of ZIF-67 and Pt/ZIF-67 composite materials prepared in the present invention. The characteristic peaks at 2θ=7.4˚, 12.7˚, and 16.5˚ correspond to the ZIF-67 crystal planes (011), (112), (013), indicating that the ZIF-67 framework is well preserved during the catalyst preparation process structure. In addition, no obvious Pt metal diffraction characteristic peaks were found from the PXRD pattern of Pt/ZIF-67, which may be due to the good dispersion of metal nanoparticles and low metal loading.
如图2为本发明所制备的Pt/ZIF-67复合材料的透射电镜图。从图2可以看出,大多数Pt纳米粒子(黑点)分布在ZIF-67的外表面上,从图3可知,Pt纳米粒子的平均尺寸为1-2nm。Figure 2 is a transmission electron microscope image of the Pt/ZIF-67 composite material prepared in the present invention. It can be seen from Figure 2 that most of the Pt nanoparticles (black dots) are distributed on the outer surface of ZIF-67, and from Figure 3 that the average size of the Pt nanoparticles is 1-2 nm.
如图4为本发明所制备的Pt/ZIF-67复合材料在不同温度下催化氨硼烷水解的放氢速率图及阿伦尼乌斯曲线。测试结果如图所示,Pt/ZIF-67复合材料的TOF为72.29 molH2 min-1 Pt mol-1,活化能通过结算可得,为39.42 kJ mol-1,如图5所示。Figure 4 shows the hydrogen desorption rate diagram and Arrhenius curve of the Pt/ZIF-67 composite material prepared in the present invention to catalyze the hydrolysis of ammonia borane at different temperatures. The test results are shown in the figure. The TOF of the Pt/ZIF-67 composite is 72.29 molH 2 min -1 Pt mol -1 , and the activation energy is 39.42 kJ mol -1 , as shown in Figure 5.
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