CN111701596B - A method for preparing an atomic-scale active site catalyst for ammonia synthesis under mild conditions - Google Patents
A method for preparing an atomic-scale active site catalyst for ammonia synthesis under mild conditions Download PDFInfo
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- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 title claims abstract description 116
- 239000003054 catalyst Substances 0.000 title claims abstract description 76
- 229910021529 ammonia Inorganic materials 0.000 title claims abstract description 58
- 238000003786 synthesis reaction Methods 0.000 title claims abstract description 50
- 230000015572 biosynthetic process Effects 0.000 title claims abstract description 46
- 238000000034 method Methods 0.000 title description 16
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims abstract description 36
- 229910021389 graphene Inorganic materials 0.000 claims abstract description 29
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 claims abstract description 26
- 239000002131 composite material Substances 0.000 claims abstract description 24
- 238000002360 preparation method Methods 0.000 claims abstract description 24
- 230000000694 effects Effects 0.000 claims abstract description 22
- 229910052757 nitrogen Inorganic materials 0.000 claims abstract description 13
- 239000001257 hydrogen Substances 0.000 claims abstract description 10
- 229910052739 hydrogen Inorganic materials 0.000 claims abstract description 10
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 claims abstract description 9
- 239000011259 mixed solution Substances 0.000 claims description 151
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Chemical compound O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 64
- 239000008367 deionised water Substances 0.000 claims description 56
- 229910021641 deionized water Inorganic materials 0.000 claims description 56
- 239000000243 solution Substances 0.000 claims description 51
- 239000011521 glass Substances 0.000 claims description 42
- 238000003756 stirring Methods 0.000 claims description 42
- UMGDCJDMYOKAJW-UHFFFAOYSA-N thiourea Chemical compound NC(N)=S UMGDCJDMYOKAJW-UHFFFAOYSA-N 0.000 claims description 42
- 238000012546 transfer Methods 0.000 claims description 24
- XSQUKJJJFZCRTK-UHFFFAOYSA-N Urea Natural products NC(N)=O XSQUKJJJFZCRTK-UHFFFAOYSA-N 0.000 claims description 21
- 150000001875 compounds Chemical class 0.000 claims description 21
- 229910002804 graphite Inorganic materials 0.000 claims description 21
- 239000010439 graphite Substances 0.000 claims description 21
- 239000005457 ice water Substances 0.000 claims description 21
- 239000012286 potassium permanganate Substances 0.000 claims description 21
- 235000015393 sodium molybdate Nutrition 0.000 claims description 21
- 239000011684 sodium molybdate Substances 0.000 claims description 21
- TVXXNOYZHKPKGW-UHFFFAOYSA-N sodium molybdate (anhydrous) Chemical compound [Na+].[Na+].[O-][Mo]([O-])(=O)=O TVXXNOYZHKPKGW-UHFFFAOYSA-N 0.000 claims description 21
- 239000006228 supernatant Substances 0.000 claims description 21
- 238000006243 chemical reaction Methods 0.000 claims description 20
- 230000002687 intercalation Effects 0.000 claims description 15
- 238000009830 intercalation Methods 0.000 claims description 15
- NWZSZGALRFJKBT-KNIFDHDWSA-N (2s)-2,6-diaminohexanoic acid;(2s)-2-hydroxybutanedioic acid Chemical compound OC(=O)[C@@H](O)CC(O)=O.NCCCC[C@H](N)C(O)=O NWZSZGALRFJKBT-KNIFDHDWSA-N 0.000 claims description 14
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 claims description 14
- IKDUDTNKRLTJSI-UHFFFAOYSA-N hydrazine monohydrate Substances O.NN IKDUDTNKRLTJSI-UHFFFAOYSA-N 0.000 claims description 14
- QAOWNCQODCNURD-UHFFFAOYSA-N sulfuric acid Substances OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 claims description 14
- 238000001291 vacuum drying Methods 0.000 claims description 14
- 230000003197 catalytic effect Effects 0.000 claims description 13
- 238000006460 hydrolysis reaction Methods 0.000 claims description 11
- 238000012360 testing method Methods 0.000 claims description 11
- 238000005259 measurement Methods 0.000 claims description 10
- 239000000047 product Substances 0.000 claims description 10
- 239000013049 sediment Substances 0.000 claims description 10
- 239000012495 reaction gas Substances 0.000 claims description 9
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 claims description 7
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical group C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 claims description 7
- 239000012279 sodium borohydride Substances 0.000 claims description 7
- 229910000033 sodium borohydride Inorganic materials 0.000 claims description 7
- 229910001220 stainless steel Inorganic materials 0.000 claims description 7
- 239000010935 stainless steel Substances 0.000 claims description 7
- 239000000203 mixture Substances 0.000 claims description 5
- 239000006185 dispersion Substances 0.000 abstract description 4
- 238000005265 energy consumption Methods 0.000 abstract description 4
- 238000001179 sorption measurement Methods 0.000 abstract description 4
- BASFCYQUMIYNBI-UHFFFAOYSA-N platinum Chemical compound [Pt] BASFCYQUMIYNBI-UHFFFAOYSA-N 0.000 abstract 4
- CWQXQMHSOZUFJS-UHFFFAOYSA-N molybdenum disulfide Chemical compound S=[Mo]=S CWQXQMHSOZUFJS-UHFFFAOYSA-N 0.000 abstract 1
- 229910052982 molybdenum disulfide Inorganic materials 0.000 abstract 1
- 229910052697 platinum Inorganic materials 0.000 abstract 1
- 239000010410 layer Substances 0.000 description 24
- 230000008569 process Effects 0.000 description 7
- 239000011229 interlayer Substances 0.000 description 6
- 239000000126 substance Substances 0.000 description 6
- 230000007062 hydrolysis Effects 0.000 description 5
- 230000001699 photocatalysis Effects 0.000 description 5
- 241000282326 Felis catus Species 0.000 description 4
- 238000010521 absorption reaction Methods 0.000 description 4
- 238000011156 evaluation Methods 0.000 description 4
- 230000007246 mechanism Effects 0.000 description 4
- 239000002244 precipitate Substances 0.000 description 4
- 230000004913 activation Effects 0.000 description 3
- 238000001994 activation Methods 0.000 description 3
- 238000004178 biological nitrogen fixation Methods 0.000 description 3
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 2
- 230000004888 barrier function Effects 0.000 description 2
- 230000003592 biomimetic effect Effects 0.000 description 2
- 238000007036 catalytic synthesis reaction Methods 0.000 description 2
- 238000010494 dissociation reaction Methods 0.000 description 2
- 230000005593 dissociations Effects 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 239000002135 nanosheet Substances 0.000 description 2
- 239000011541 reaction mixture Substances 0.000 description 2
- 229910017116 Fe—Mo Inorganic materials 0.000 description 1
- 238000009620 Haber process Methods 0.000 description 1
- 108010020943 Nitrogenase Proteins 0.000 description 1
- 238000009825 accumulation Methods 0.000 description 1
- 230000002776 aggregation Effects 0.000 description 1
- 238000004220 aggregation Methods 0.000 description 1
- 239000007864 aqueous solution Substances 0.000 description 1
- 239000001569 carbon dioxide Substances 0.000 description 1
- 229910002092 carbon dioxide Inorganic materials 0.000 description 1
- 239000003575 carbonaceous material Substances 0.000 description 1
- 238000006555 catalytic reaction Methods 0.000 description 1
- 239000007806 chemical reaction intermediate Substances 0.000 description 1
- 230000002860 competitive effect Effects 0.000 description 1
- 230000008094 contradictory effect Effects 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 150000002431 hydrogen Chemical class 0.000 description 1
- 238000005984 hydrogenation reaction Methods 0.000 description 1
- 238000001027 hydrothermal synthesis Methods 0.000 description 1
- 238000002329 infrared spectrum Methods 0.000 description 1
- 230000003993 interaction Effects 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 229910000510 noble metal Inorganic materials 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 239000000376 reactant Substances 0.000 description 1
- 230000009467 reduction Effects 0.000 description 1
- 230000005476 size effect Effects 0.000 description 1
- 241000894007 species Species 0.000 description 1
- 230000002195 synergetic effect Effects 0.000 description 1
- 229910052723 transition metal Inorganic materials 0.000 description 1
- 150000003624 transition metals Chemical class 0.000 description 1
Classifications
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J27/00—Catalysts comprising the elements or compounds of halogens, sulfur, selenium, tellurium, phosphorus or nitrogen; Catalysts comprising carbon compounds
- B01J27/02—Sulfur, selenium or tellurium; Compounds thereof
- B01J27/04—Sulfides
- B01J27/047—Sulfides with chromium, molybdenum, tungsten or polonium
- B01J27/051—Molybdenum
- B01J27/0515—Molybdenum with iron group metals or platinum group metals
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J27/00—Catalysts comprising the elements or compounds of halogens, sulfur, selenium, tellurium, phosphorus or nitrogen; Catalysts comprising carbon compounds
- B01J27/02—Sulfur, selenium or tellurium; Compounds thereof
- B01J27/04—Sulfides
- B01J27/047—Sulfides with chromium, molybdenum, tungsten or polonium
- B01J27/051—Molybdenum
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J35/00—Catalysts, in general, characterised by their form or physical properties
- B01J35/30—Catalysts, in general, characterised by their form or physical properties characterised by their physical properties
- B01J35/391—Physical properties of the active metal ingredient
- B01J35/394—Metal dispersion value, e.g. percentage or fraction
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01C—AMMONIA; CYANOGEN; COMPOUNDS THEREOF
- C01C1/00—Ammonia; Compounds thereof
- C01C1/02—Preparation, purification or separation of ammonia
- C01C1/04—Preparation of ammonia by synthesis in the gas phase
- C01C1/0405—Preparation of ammonia by synthesis in the gas phase from N2 and H2 in presence of a catalyst
- C01C1/0411—Preparation of ammonia by synthesis in the gas phase from N2 and H2 in presence of a catalyst characterised by the catalyst
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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
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P20/00—Technologies relating to chemical industry
- Y02P20/50—Improvements relating to the production of bulk chemicals
- Y02P20/52—Improvements relating to the production of bulk chemicals using catalysts, e.g. selective catalysts
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- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
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Abstract
本发明公开了一种能够在温和条件下催化氮气氢气合成氨气的原子级活性位点催化剂的制备方法,该催化剂以还原氧化石墨烯(RGO)和二硫化钼(MoS2)为复合载体、原子级分散的铂(Pt)为活性组分,合成的Pt‑MoS2/RGO催化剂可以显著提高合成氨的速率。复合载体具有MoS2的强吸附性能以及RGO良好的导电性能,MoS2以多层形式沉积在RGO表面,两者形成了连续的电子传输网络,原子级的Pt均匀分散在复合载体上,达到了原子分散的极限,显著提高了合成氨反应的活性与稳定性,使合成氨反应能够在温和条件下驱动,降低了传统合成氨工业的能耗。The invention discloses a preparation method of an atomic-level active site catalyst capable of catalyzing the synthesis of ammonia from nitrogen and hydrogen under mild conditions. The catalyst uses reduced graphene oxide (RGO) and molybdenum disulfide (MoS 2 ) as composite supports, atomic The grade-dispersed platinum (Pt) is the active component, and the synthesized Pt‑MoS 2 /RGO catalyst can significantly increase the rate of ammonia synthesis. The composite carrier has the strong adsorption performance of MoS 2 and the good conductivity of RGO. MoS 2 is deposited on the surface of RGO in a multi-layer form, and the two form a continuous electron transport network. The atomic-level Pt is evenly dispersed on the composite carrier, achieving The limit of atomic dispersion significantly improves the activity and stability of the ammonia synthesis reaction, enables the ammonia synthesis reaction to be driven under mild conditions, and reduces the energy consumption of the traditional ammonia synthesis industry.
Description
技术领域technical field
本发明属于合成氨催化剂制备方法领域,具体涉及一种在温和条件下催化氮气氢气合成氨气的原子级活性位点催化剂的制备方法。The invention belongs to the field of preparation methods of ammonia synthesis catalysts, and in particular relates to a preparation method of an atomic-level active site catalyst that catalyzes synthesis of ammonia from nitrogen and hydrogen under mild conditions.
背景技术Background technique
氨的工业合成主要依赖于能源密集型的Haber-Bosch工艺,该工艺要求高温(300~550℃)、高压(15~25MPa)操作条件,是一个高能耗、高二氧化碳排放的过程。为了降低能耗,人们开始在温和条件下对合成氨进行探索。The industrial synthesis of ammonia mainly relies on the energy-intensive Haber-Bosch process, which requires high temperature (300-550°C) and high-pressure (15-25MPa) operating conditions, and is a process with high energy consumption and high carbon dioxide emissions. In order to reduce energy consumption, people began to explore synthetic ammonia under mild conditions.
目前主流的在温和条件下合成氨技术有光催化合成氨、电催化合成氨、人工仿生催化合成氨及热催化合成氨。利用太阳能光催化合成氨技术,受限于氮气分子极高的化学稳定性带来的对于氮气分子的吸附,活化和解离过程的限制,这导致光催化合成氨的产率较低。此外,氮气分子在水溶液中极低的溶解度以及水氧化反应缓慢的动力学特征,限制了反应物氮气和质子的供应,进一步影响光催化合成氨的效率。光催化合成氨过程中还存在大量的可见-红外光谱区域太阳光被浪费的问题,太阳能-化学能转换过程效率普遍较低。电催化合成氨借助外部输入的电能实现温和条件下合成氨,具有降低能耗,清洁无污染等优点。科研人员通过对催化剂进行修饰改性、加入助催化剂等方法希望提高电催化合成氨性能,但是电催化合成氨受限于析氢反应(HER)电位和氮还原电位非常接近带来的竞争性析氢反应,产氨速率和法拉第电流效率仍然偏低,未来需要研发更高效的非贵金属催化剂提高电化学合成氨性能。人工仿生催化合成氨是通过人工的方法模拟自然界中生物固氮酶的Fe-Mo协同催化机制。不同于传统的工业合成氨过程,生物固氮可以在温和条件下进行,不受多相热催化合成氨高温高压催化条件的限制,以优先结合加氢机制降低N2的活化能垒,并规避–Evans–Polanyi(BEP)关系的限制。但是,由于人们对于生物固氮机理还未完全了解,目前在温和条件下通过人工模拟生物固氮机制合成氨效率仍旧很低,并不适合大规模推广应用。在传统热催化过程中,多利用过渡金属催化剂催化氮气氢气合成氨气,但N2分子解离会受到BEP关系的限制,N2分子活化势垒与反应中间物种吸附能间存在矛盾关系,一个理想的合成氨催化剂应该能平衡两者之间的关系,在火山型曲线的顶部附近。在热催化合成氨过程中,需要打破BEP关系的限制,才有可能实现氨的高效合成。At present, the mainstream ammonia synthesis technologies under mild conditions include photocatalytic ammonia synthesis, electrocatalytic ammonia synthesis, artificial biomimetic catalytic ammonia synthesis and thermal catalytic ammonia synthesis. The use of solar photocatalytic ammonia synthesis technology is limited by the extremely high chemical stability of nitrogen molecules, which limits the adsorption, activation and dissociation process of nitrogen molecules, which leads to a low yield of photocatalytic ammonia synthesis. In addition, the extremely low solubility of nitrogen molecules in aqueous solution and the slow kinetic characteristics of water oxidation reaction limit the supply of reactant nitrogen and protons, further affecting the efficiency of photocatalytic ammonia synthesis. In the process of photocatalytic ammonia synthesis, there is also the problem that a large amount of sunlight in the visible-infrared spectrum region is wasted, and the efficiency of the solar-chemical energy conversion process is generally low. The electrocatalytic synthesis of ammonia realizes the synthesis of ammonia under mild conditions with the help of external input electric energy, which has the advantages of reducing energy consumption, clean and pollution-free. Researchers hope to improve the performance of electrocatalytic ammonia synthesis by modifying the catalyst and adding cocatalysts. However, the electrocatalytic ammonia synthesis is limited by the competitive hydrogen evolution reaction brought about by the close proximity of the hydrogen evolution reaction (HER) potential and the nitrogen reduction potential. The ammonia rate and faradaic current efficiency are still low. In the future, it is necessary to develop more efficient non-noble metal catalysts to improve the performance of electrochemical synthesis of ammonia. Artificial biomimetic catalytic synthesis of ammonia is an artificial method to simulate the Fe-Mo synergistic catalytic mechanism of biological nitrogenase in nature. Different from the traditional industrial ammonia synthesis process, biological nitrogen fixation can be carried out under mild conditions, not limited by the high-temperature and high-pressure catalytic conditions of heterogeneous thermal catalytic ammonia synthesis, so as to preferentially combine the hydrogenation mechanism to reduce the activation energy barrier of N2 and avoid – Limitations of the Evans–Polanyi (BEP) relationship. However, since the mechanism of biological nitrogen fixation is not yet fully understood, the efficiency of ammonia synthesis under mild conditions is still very low by artificially simulating the mechanism of biological nitrogen fixation, which is not suitable for large-scale application. In the traditional thermocatalytic process, transition metal catalysts are often used to catalyze the synthesis of ammonia from nitrogen and hydrogen, but the dissociation of N2 molecules will be limited by the BEP relationship, and there is a contradictory relationship between the activation barrier of N2 molecules and the adsorption energy of reaction intermediate species. An ideal A good ammonia synthesis catalyst should balance the relationship between the two, near the top of the volcano-type curve. In the process of thermocatalytic ammonia synthesis, it is necessary to break the limitation of the BEP relationship in order to achieve efficient synthesis of ammonia.
发明内容Contents of the invention
本发明的目的在于克服已有技术的缺点,提供一种在温和条件下催化氮气氢气合成氨气的原子级活性位点催化剂制备方法。合成的Pt-MoS2/RGO催化剂可以显著提高合成氨反应的活性与稳定性,使合成氨反应能够在温和条件下驱动。The purpose of the present invention is to overcome the shortcomings of the prior art and provide a method for preparing an atomic-level active site catalyst that catalyzes the synthesis of ammonia from nitrogen and hydrogen under mild conditions. The synthesized Pt-MoS 2 /RGO catalyst can significantly improve the activity and stability of the ammonia synthesis reaction, enabling the ammonia synthesis reaction to be driven under mild conditions.
为了实现上述目的,本发明采用如下技术方案:In order to achieve the above object, the present invention adopts the following technical solutions:
本发明的一种在温和条件下催化氮气氢气合成氨气原子级活性位点催化剂,包括以下步骤:An atomic-level active site catalyst for catalyzing the synthesis of ammonia from nitrogen and hydrogen under mild conditions of the present invention comprises the following steps:
一种在温和条件下催化氮气氢气合成氨气原子级活性位点催化剂,其特征在于包括以下步骤:An atomic-level active site catalyst that catalyzes the synthesis of ammonia from nitrogen and hydrogen under mild conditions is characterized in that it comprises the following steps:
步骤一、还原氧化石墨烯载体的制备:Step 1, preparation of reduced graphene oxide carrier:
(1)在0~4℃冰水浴条件下,将50~100mL质量分数为98%的浓硫酸在玻璃棒搅拌下缓慢加入圆底烧瓶中,随后缓慢加入1.0000~2.0000g NaNO3和1.0000~2.0000g石墨粉形成混合溶液;当混合溶液温度降至0~4℃后,分三次缓慢加入6.0000~12.0000g高锰酸钾,待最后一次加入高锰酸钾后在0~4℃冰水浴中恒温反应20~40min,氧化石墨粉形成硫酸-石墨层间化合物,此时得到的混合溶液记为混合溶液A;撤除冰水浴使混合溶液A温度上升至20~25℃后继续反应1~3h,深度氧化硫酸-石墨层间化合物,此时得到的混合溶液记为混合溶液B;(1) Under the condition of ice-water bath at 0-4°C, slowly add 50-100mL of concentrated sulfuric acid with a mass fraction of 98% into a round-bottomed flask under stirring with a glass rod, and then slowly add 1.0000-2.0000g NaNO 3 and 1.0000-2.0000 g of graphite powder to form a mixed solution; when the temperature of the mixed solution drops to 0-4°C, slowly add 6.0000-12.0000g of potassium permanganate three times, and keep the temperature in an ice-water bath at 0-4°C after adding potassium permanganate for the last time After reacting for 20-40 minutes, the graphite oxide powder forms a sulfuric acid-graphite intercalation compound. The mixed solution obtained at this time is recorded as mixed solution A; remove the ice-water bath to raise the temperature of the mixed solution A to 20-25°C and continue the reaction for 1-3 hours. Oxidized sulfuric acid-graphite intercalation compound, the mixed solution that obtains this moment is denoted as mixed solution B;
(2)将60~100mL去离子水加入混合溶液B中,利用步骤(1)中加入的残余的浓硫酸与水作用时放出的热量使混合溶液B的温度逐渐升至96~100℃,然后在玻璃棒搅拌下反应0.3~0.7h,使混合溶液B中的硫酸-石墨层间化合物发生水解反应;向水解后的混合溶液中加入5~25mL质量分数为10~30%的H2O2溶液,除去过量的高锰酸钾,得到的溶液记为混合溶液C;然后将混合溶液C转移至8000~12000r/min的高速离心机中离心10~40min,倒掉离心管上层清液,离心管下层沉淀物即为氧化石墨烯;(2) Add 60-100 mL of deionized water into the mixed solution B, use the heat released when the residual concentrated sulfuric acid added in step (1) interacts with water to gradually increase the temperature of the mixed solution B to 96-100 °C, and then React for 0.3~0.7h under stirring with a glass rod, so that the sulfuric acid-graphite intercalation compound in the mixed solution B undergoes hydrolysis reaction; add 5~25mL of H 2 O 2 with a mass fraction of 10~30% to the hydrolyzed mixed solution Solution, remove excess potassium permanganate, and the obtained solution is recorded as mixed solution C; then transfer the mixed solution C to a high-speed centrifuge at 8000-12000r/min for 10-40min, pour off the supernatant of the centrifuge tube, and centrifuge The sediment in the lower layer of the tube is graphene oxide;
(3)将离心管下层的氧化石墨烯移至烧杯中,依次向烧杯中加入60~100mL去离子水、30~60mL纯净的水合肼,并用玻璃棒搅拌均匀得到混合溶液D;将混合溶液D置于100~140℃真空干燥箱中反应8~10h,得到RGO载体,将RGO载体用去离子水洗涤三次,除去残余的水合肼后再次放入真空干燥箱中,于100~140℃下干燥1~3h,得到纯净的RGO载体;(3) Move the graphene oxide in the lower layer of the centrifuge tube to a beaker, add 60-100mL deionized water and 30-60mL pure hydrazine hydrate to the beaker in turn, and stir with a glass rod to obtain a mixed solution D; Put it in a vacuum drying oven at 100-140°C for 8-10 hours to obtain the RGO carrier, wash the RGO carrier with deionized water three times, remove the residual hydrazine hydrate, put it in a vacuum drying oven again, and dry it at 100-140°C 1 to 3 hours to obtain pure RGO carrier;
步骤二、MoS2/RGO复合载体的制备:Step 2. Preparation of MoS 2 /RGO composite carrier:
(1)将0.0024~0.0048g纯净的RGO载体置于烧杯中,加入60~100mL去离子水,用超声波清洗机超声处理10~30min使纯净的RGO全部溶解,得到RGO混合溶液;(1) Put 0.0024-0.0048g of pure RGO carrier in a beaker, add 60-100mL of deionized water, and use an ultrasonic cleaner to sonicate for 10-30min to completely dissolve the pure RGO to obtain a mixed solution of RGO;
(2)将0.0242g钼酸钠加入RGO溶液中并用玻璃棒搅拌均匀得到溶有钼酸钠的RGO混合溶液;将硫脲0.0076~0.0380g溶于40~60mL去离子水中得到硫脲溶液;用滴管将该硫脲溶液缓慢滴入溶有钼酸钠的RGO混合溶液中,用玻璃棒搅拌均匀后加入质量分数为10%的盐酸溶液调节pH值为0.1~7,得到混合溶液E;(2) 0.0242g sodium molybdate is added in the RGO solution and is evenly stirred with a glass rod to obtain the RGO mixed solution that is dissolved with sodium molybdate; 0.0076~0.0380g of thiourea is dissolved in 40~60mL deionized water to obtain a thiourea solution; Slowly drop the thiourea solution into the RGO mixed solution dissolved in sodium molybdate with a dropper, stir evenly with a glass rod, and then add hydrochloric acid solution with a mass fraction of 10% to adjust the pH value to 0.1-7 to obtain a mixed solution E;
(3)将混合溶液E转移至聚四氟乙烯内衬的不锈钢反应釜中,在100~250℃条件下生长MoS2,生长18~30h后取出,转移至8000~12000r/min的高速离心机中离心10~40min,然后倒掉离心管上层清液,离心管下层沉淀物即为MoS2/RGO,将MoS2/RGO产物用去离子水洗涤三次,置于100~140℃真空干燥箱中干燥1~3h,得到MoS2/RGO复合载体;(3) Transfer the mixed solution E to a polytetrafluoroethylene-lined stainless steel reactor, grow MoS 2 at 100-250°C, take it out after 18-30 hours of growth, and transfer it to a high-speed centrifuge at 8000-12000r/min Centrifuge for 10-40min, then pour off the supernatant of the centrifuge tube, the sediment in the lower layer of the centrifuge tube is MoS 2 /RGO, wash the MoS 2 /RGO product with deionized water three times, and place it in a vacuum oven at 100-140°C Dry for 1-3 hours to obtain MoS 2 /RGO composite carrier;
步骤三、Pt-MoS2/RGO催化剂的制备:Step 3. Preparation of Pt-MoS 2 /RGO catalyst:
(1)将0.0200~0.0800gMoS2/RGO复合载体置于烧杯中,加入60~100mL去离子水,用超声波清洗机超声处理10~30min使MoS2/RGO全部溶解,得到混合溶液F;(1) Put 0.0200-0.0800g of MoS 2 /RGO composite carrier in a beaker, add 60-100mL of deionized water, and use an ultrasonic cleaner to sonicate for 10-30 minutes to completely dissolve MoS 2 /RGO, and obtain a mixed solution F;
(2)将0.0020~0.0100g H2PtCl6·6H2O加入60~100mL混合溶液F中并搅拌均匀,然后在20~25℃下用滴管向其中逐滴滴加60~100mL 0.5mol/L硼氢化钠溶液,滴加的同时用玻璃棒搅拌均匀,得到反应后的混合物转移至8000~12000r/min的高速离心机中离心10~40min,倒掉离心管上层清液,离心管下层物质即为Pt-MoS2/RGO催化剂;将Pt-MoS2/RGO催化剂分别用去离子水和质量分数为10~30%的无水乙醇洗涤三次后置于160~240℃真空干燥箱中干燥2~5h,得到纯净的Pt-MoS2/RGO催化剂。(2) Add 0.0020~0.0100g H 2 PtCl 6 ·6H 2 O into 60~100mL mixed solution F and stir evenly, then add 60~100mL 0.5mol/ L sodium borohydride solution, stir evenly with a glass rod while adding dropwise, transfer the reacted mixture to a high-speed centrifuge at 8000-12000r/min for 10-40min, pour off the supernatant of the centrifuge tube, and the lower layer of the centrifuge tube It is the Pt-MoS 2 /RGO catalyst; the Pt-MoS 2 /RGO catalyst was washed three times with deionized water and absolute ethanol with a mass fraction of 10-30%, and then dried in a vacuum oven at 160-240°C for 2 ~5h, a pure Pt-MoS 2 /RGO catalyst was obtained.
与现有技术相比,本发明具有以下优点:Compared with the prior art, the present invention has the following advantages:
(1)Pt的原子级分散。MoS2的活性位点仅位于MoS2片层边缘,片层的面内则表现出化学惰性,这限制了其广泛应用,为了进一步提高活性位点的数量,增加合成氨的性能,引入原子级分散的Pt。当Pt分散度达到原子尺寸时能够引起诸如表面自由能、量子尺寸效应、不饱和配位环境和金属-载体相互作用等性质发生急剧变化,显著提高催化剂的合成氨性能。(1) Atomic-scale dispersion of Pt. The active sites of MoS 2 are only located on the edge of the MoS 2 sheet, and the inside of the sheet is chemically inert, which limits its wide application. In order to further increase the number of active sites and increase the performance of ammonia synthesis, the introduction of atomic-level dispersion Pt. When the Pt dispersion reaches the atomic size, it can cause drastic changes in properties such as surface free energy, quantum size effect, unsaturated coordination environment, and metal-support interaction, which can significantly improve the ammonia synthesis performance of the catalyst.
(2)催化剂载体的空间限域效应。MoS2边缘存在大量悬键能够为催化反应提供更多的吸附位点,还原氧化石墨烯表面存在的缺陷为MoS2的生长提供了位点,使MoS2生长在还原氧化石墨烯表面。将碳材料加入到水热反应体系中,能够在溶液中形成空间位阻效应,可以抑制MoS2纳米片层的堆积,同时也在空间限制了MoS2纳米片的聚集,进而提高了材料的比表面积,产生更多的活性位点,实现温和条件下高效催化合成氨。(2) The spatial confinement effect of the catalyst support. The presence of a large number of dangling bonds on the edge of MoS 2 can provide more adsorption sites for catalytic reactions, and the defects on the surface of reduced graphene oxide provide sites for the growth of MoS 2 , so that MoS 2 grows on the surface of reduced graphene oxide. Adding carbon materials into the hydrothermal reaction system can form a steric hindrance effect in the solution, which can inhibit the accumulation of MoS 2 nanosheets, and at the same time limit the aggregation of MoS 2 nanosheets in space, thereby improving the specificity of the material. Larger surface area, more active sites, and efficient catalytic synthesis of ammonia under mild conditions.
具体实施方式Detailed ways
为了使发明所述的案例更易于理解,列举以下具体实施例,但是本发明的权利要求范围不受这些实施例的限制。基于本发明的实施例,本领域普通技术人员在没有做出创造性劳动前提下所获得的所有其他实施例,都属于本发明保护的范围。In order to make the cases described in the invention easier to understand, the following specific examples are listed, but the scope of the claims of the present invention is not limited by these examples. Based on the embodiments of the present invention, all other embodiments obtained by persons of ordinary skill in the art without making creative efforts fall within the protection scope of the present invention.
本发明的一种用于温和条件下催化氮气氢气合成氨气的原子级活性位点催化剂,包括以下步骤:An atomic-level active site catalyst for catalyzing the synthesis of ammonia from nitrogen and hydrogen under mild conditions of the present invention comprises the following steps:
步骤一、还原氧化石墨烯载体的制备:Step 1, preparation of reduced graphene oxide carrier:
(1)在0~4℃冰水浴条件下,将50~100mL质量分数为98%的浓硫酸在玻璃棒搅拌下缓慢加入圆底烧瓶中,随后缓慢加入1.0000~2.0000g NaNO3和1.0000~2.0000g石墨粉形成混合溶液;当混合溶液温度降至0~4℃后,分三次缓慢加入6.0000~12.0000g高锰酸钾,待最后一次加入高锰酸钾后在0~4℃冰水浴中恒温反应20~40min,氧化石墨粉形成硫酸-石墨层间化合物,此时得到的混合溶液记为混合溶液A;撤除冰水浴使混合溶液A温度上升至20~25℃后继续反应1~3h,深度氧化硫酸-石墨层间化合物,此时得到的混合溶液记为混合溶液B。(1) Under the condition of ice-water bath at 0-4°C, slowly add 50-100mL of concentrated sulfuric acid with a mass fraction of 98% into a round-bottomed flask under stirring with a glass rod, and then slowly add 1.0000-2.0000g NaNO 3 and 1.0000-2.0000 g of graphite powder to form a mixed solution; when the temperature of the mixed solution drops to 0-4°C, slowly add 6.0000-12.0000g of potassium permanganate three times, and keep the temperature in an ice-water bath at 0-4°C after adding potassium permanganate for the last time After reacting for 20-40 minutes, the graphite oxide powder forms a sulfuric acid-graphite intercalation compound. The mixed solution obtained at this time is recorded as mixed solution A; remove the ice-water bath to raise the temperature of the mixed solution A to 20-25°C and continue the reaction for 1-3 hours. Oxidize the sulfuric acid-graphite intercalation compound, and the mixed solution obtained at this time is denoted as mixed solution B.
(2)将60~100mL去离子水加入混合溶液B中,利用步骤(1)中加入的残余的浓硫酸与水作用时放出的热量使混合溶液B的温度逐渐升至96~100℃,然后在玻璃棒搅拌下反应0.3~0.7h,使混合溶液B中的硫酸-石墨层间化合物发生水解反应。向水解后的混合溶液中加入5~25mL质量分数为10~30%的H2O2溶液,除去过量的高锰酸钾,得到的溶液记为混合溶液C;然后将混合溶液C转移至8000~12000r/min的高速离心机中离心10~40min,倒掉离心管上层清液,离心管下层沉淀物即为氧化石墨烯。(2) Add 60-100 mL of deionized water into the mixed solution B, use the heat released when the residual concentrated sulfuric acid added in step (1) interacts with water to gradually increase the temperature of the mixed solution B to 96-100 °C, and then React for 0.3-0.7 h under stirring with a glass rod, so that the sulfuric acid-graphite intercalation compound in the mixed solution B undergoes a hydrolysis reaction. Add 5 to 25 mL of H2O2 solution with a mass fraction of 10 to 30% to the mixed solution after hydrolysis, remove excess potassium permanganate, and record the obtained solution as mixed solution C; then transfer mixed solution C to 8000 Centrifuge in a high-speed centrifuge at ~12000r/min for 10-40min, pour off the supernatant of the centrifuge tube, and the sediment in the lower layer of the centrifuge tube is graphene oxide.
(3)将离心管下层的氧化石墨烯移至烧杯中,依次向烧杯中加入60~100mL去离子水、30~60mL纯净的水合肼,并用玻璃棒搅拌均匀得到混合溶液D;将混合溶液D置于100~140℃真空干燥箱中反应8~10h,得到RGO(还原氧化石墨烯)载体,将RGO载体用去离子水洗涤三次,除去残余的水合肼后再次放入真空干燥箱中,于100~140℃下干燥1~3h,得到纯净的RGO载体。(3) Move the graphene oxide in the lower layer of the centrifuge tube to a beaker, add 60-100mL deionized water and 30-60mL pure hydrazine hydrate to the beaker in turn, and stir with a glass rod to obtain a mixed solution D; Put it in a vacuum drying oven at 100-140°C for 8-10 hours to obtain the RGO (reduced graphene oxide) carrier, wash the RGO carrier with deionized water three times, remove the residual hydrazine hydrate, and then put it in the vacuum drying oven again. Dry at 100-140° C. for 1-3 hours to obtain a pure RGO carrier.
步骤二、MoS2/RGO复合载体的制备:Step 2. Preparation of MoS 2 /RGO composite carrier:
(1)将0.0024~0.0048g纯净的RGO载体置于烧杯中,加入60~100mL去离子水,用超声波清洗机超声处理10~30min使纯净的RGO全部溶解,得到RGO混合溶液。(1) Put 0.0024-0.0048 g of pure RGO carrier in a beaker, add 60-100 mL of deionized water, and use an ultrasonic cleaner to sonicate for 10-30 minutes to completely dissolve the pure RGO to obtain a mixed solution of RGO.
(2)将0.0242g钼酸钠加入RGO溶液中并用玻璃棒搅拌均匀得到溶有钼酸钠的RGO混合溶液;将硫脲0.0076~0.0380g溶于40~60mL去离子水中得到硫脲溶液;用滴管将该硫脲溶液缓慢滴入溶有钼酸钠的RGO混合溶液中,用玻璃棒搅拌均匀后加入质量分数为10%的盐酸溶液调节pH值为0.1~7,得到混合溶液E。(2) 0.0242g sodium molybdate is added in the RGO solution and is evenly stirred with a glass rod to obtain the RGO mixed solution that is dissolved with sodium molybdate; 0.0076~0.0380g of thiourea is dissolved in 40~60mL deionized water to obtain a thiourea solution; Slowly drop the thiourea solution into the RGO mixed solution dissolved in sodium molybdate with a dropper, stir evenly with a glass rod, and then add 10% hydrochloric acid solution to adjust the pH to 0.1-7 to obtain mixed solution E.
(3)将混合溶液E转移至聚四氟乙烯内衬的不锈钢反应釜中,在100~250℃条件下生长MoS2,生长18~30h后取出,转移至8000~12000r/min的高速离心机中离心10~40min,然后倒掉离心管上层清液,离心管下层沉淀物即为MoS2/RGO,将MoS2/RGO产物用去离子水洗涤三次,置于100~140℃真空干燥箱中干燥1~3h,得到MoS2/RGO复合载体。(3) Transfer the mixed solution E to a polytetrafluoroethylene-lined stainless steel reactor, grow MoS 2 at 100-250°C, take it out after 18-30 hours of growth, and transfer it to a high-speed centrifuge at 8000-12000r/min Centrifuge for 10-40min, then pour off the supernatant of the centrifuge tube, the sediment in the lower layer of the centrifuge tube is MoS 2 /RGO, wash the MoS 2 /RGO product with deionized water three times, and place it in a vacuum oven at 100-140°C Dry for 1-3 hours to obtain the MoS 2 /RGO composite carrier.
步骤三、Pt-MoS2/RGO催化剂的制备:Step 3. Preparation of Pt-MoS 2 /RGO catalyst:
(1)将0.0200~0.0800gMoS2/RGO复合载体置于烧杯中,加入60~100mL去离子水,用超声波清洗机超声处理10~30min使MoS2/RGO全部溶解,得到混合溶液F。(1) Put 0.0200-0.0800g of MoS 2 /RGO composite carrier in a beaker, add 60-100mL of deionized water, and use an ultrasonic cleaner to sonicate for 10-30min to completely dissolve the MoS 2 /RGO, and obtain a mixed solution F.
(2)将0.0020~0.0100g H2PtCl6·6H2O加入60~100mL混合溶液F中并搅拌均匀,然后在20~25℃下用滴管向其中逐滴滴加60~100mL 0.5mol/L硼氢化钠溶液,滴加的同时用玻璃棒搅拌均匀,得到反应后的混合物转移至8000~12000r/min的高速离心机中离心10~40min,倒掉离心管上层清液,离心管下层物质即为Pt-MoS2/RGO催化剂;将Pt-MoS2/RGO催化剂分别用去离子水和质量分数为10~30%的无水乙醇洗涤三次后置于160~240℃真空干燥箱中干燥2~5h,得到纯净的Pt-MoS2/RGO催化剂。(2) Add 0.0020~0.0100g H 2 PtCl 6 ·6H 2 O into 60~100mL mixed solution F and stir evenly, then add 60~100mL 0.5mol/ L sodium borohydride solution, stir evenly with a glass rod while adding dropwise, transfer the reacted mixture to a high-speed centrifuge at 8000-12000r/min for 10-40min, pour off the supernatant of the centrifuge tube, and the lower layer of the centrifuge tube It is the Pt-MoS 2 /RGO catalyst; the Pt-MoS 2 /RGO catalyst was washed three times with deionized water and absolute ethanol with a mass fraction of 10-30%, and then dried in a vacuum oven at 160-240°C for 2 ~5h, a pure Pt-MoS 2 /RGO catalyst was obtained.
实施例1Example 1
步骤一、还原氧化石墨烯载体的制备:Step 1, preparation of reduced graphene oxide carrier:
(1)在0℃冰水浴条件下,将50mL质量分数为98%的浓硫酸在玻璃棒搅拌下缓慢加入圆底烧瓶中,随后缓慢加入1.0000g NaNO3和1.0000g石墨粉形成混合溶液;当混合溶液温度降至0℃后,分三次缓慢加入6.0000g高锰酸钾,待最后一次加入高锰酸钾后在0℃冰水浴中恒温反应20min,氧化石墨粉形成硫酸-石墨层间化合物,此时得到的混合溶液记为混合溶液A;撤除冰水浴使混合溶液A温度上升至20℃后继续反应1h,深度氧化硫酸-石墨层间化合物,此时得到的混合溶液记为混合溶液B。(1) Under the condition of 0 ℃ of ice-water bath, the concentrated sulfuric acid that 50mL mass fraction is 98% is slowly added in the round-bottomed flask under glass rod stirring, then slowly add 1.0000g NaNO 3 and 1.0000g graphite powder form mixed solution; After the temperature of the mixed solution is lowered to 0°C, slowly add 6.0000g of potassium permanganate three times. After adding potassium permanganate for the last time, react at a constant temperature in an ice-water bath at 0°C for 20 minutes. The graphite oxide powder forms a sulfuric acid-graphite interlayer compound. The mixed solution obtained at this time was designated as mixed solution A; the ice-water bath was removed to raise the temperature of mixed solution A to 20°C, and then the reaction was continued for 1 h to deeply oxidize the sulfuric acid-graphite intercalation compound. The mixed solution obtained at this time was designated as mixed solution B.
(2)将60mL去离子水加入混合溶液B中,利用步骤(1)中加入的残余浓硫酸与水作用时放出的热量使混合溶液B的温度逐渐升至96℃,然后在玻璃棒搅拌下反应0.3h,使混合溶液B中的硫酸-石墨层间化合物发生水解反应。向水解后的混合溶液中加入5mL质量分数为10%的H2O2溶液,除去过量的高锰酸钾,得到的溶液记为混合溶液C;然后将混合溶液C转移至8000r/min的高速离心机中离心10min,倒掉离心管上层清液,离心管下层沉淀物即为氧化石墨烯。(2) Add 60mL of deionized water to the mixed solution B, use the heat released when the residual concentrated sulfuric acid added in step (1) interacts with water to gradually raise the temperature of the mixed solution B to 96°C, and then stir it with a glass rod After reacting for 0.3h, the sulfuric acid-graphite intercalation compound in the mixed solution B undergoes a hydrolysis reaction. Add 5mL of H2O2 solution with a mass fraction of 10% to the mixed solution after hydrolysis, remove excess potassium permanganate, and record the obtained solution as mixed solution C; then transfer the mixed solution C to a high-speed 8000r/min Centrifuge in a centrifuge for 10 minutes, pour off the supernatant of the centrifuge tube, and the sediment in the lower layer of the centrifuge tube is graphene oxide.
(3)将离心管下层的氧化石墨烯移至烧杯中,依次向烧杯中加入60mL去离子水、30mL纯净的水合肼,并用玻璃棒搅拌均匀得到混合溶液D;将混合溶液D置于100℃真空干燥箱中反应8h,得到RGO(还原氧化石墨烯)载体,将RGO载体用去离子水洗涤三次,除去残余的水合肼后再次放入真空干燥箱中,于100℃下干燥1h,得到纯净的RGO载体。(3) Move the graphene oxide in the lower layer of the centrifuge tube to a beaker, add 60mL deionized water and 30mL pure hydrazine hydrate to the beaker in turn, and stir with a glass rod to obtain a mixed solution D; place the mixed solution D at 100°C React in a vacuum drying oven for 8 hours to obtain an RGO (reduced graphene oxide) carrier, wash the RGO carrier three times with deionized water, remove the residual hydrazine hydrate, put it in a vacuum drying oven again, and dry it at 100°C for 1 hour to obtain pure The RGO vector.
步骤二、MoS2/RGO复合载体的制备:Step 2. Preparation of MoS 2 /RGO composite carrier:
(1)将0.0024g纯净的RGO载体置于烧杯中,加入60mL去离子水,用超声波清洗机超声处理10min使纯净的RGO全部溶解,得到RGO混合溶液。(1) Put 0.0024 g of pure RGO carrier in a beaker, add 60 mL of deionized water, and use an ultrasonic cleaner to sonicate for 10 min to completely dissolve the pure RGO to obtain a mixed solution of RGO.
(2)将0.0242g钼酸钠加入RGO溶液中并用玻璃棒搅拌均匀得到溶有钼酸钠的RGO混合溶液;将硫脲0.0076g溶解于40mL去离子水中得到硫脲溶液;用滴管将该硫脲溶液缓慢滴入溶有钼酸钠的RGO混合溶液中,用玻璃棒搅拌均匀后加入质量分数为10%的盐酸溶液调节pH值为0.1,得到混合溶液E。(2) Add 0.0242g sodium molybdate in the RGO solution and stir with a glass rod to obtain a mixed solution of RGO that is dissolved with sodium molybdate; dissolve 0.0076g of thiourea in 40mL deionized water to obtain a thiourea solution; The thiourea solution was slowly dropped into the RGO mixed solution dissolved in sodium molybdate, stirred evenly with a glass rod, and then 10% hydrochloric acid solution was added to adjust the pH value to 0.1 to obtain the mixed solution E.
(3)将混合溶液E转移至聚四氟乙烯内衬的不锈钢反应釜中,在100℃条件下生长MoS2,生长18h后取出,转移至8000r/min的高速离心机中离心10min,然后倒掉离心管上层清液,离心管下层沉淀物即为MoS2/RGO产物,将MoS2/RGO产物用去离子水洗涤三次,置于100℃真空干燥箱中干燥1h,得到MoS2/RGO复合载体。(3) Transfer the mixed solution E to a polytetrafluoroethylene-lined stainless steel reactor, grow MoS 2 at 100°C, take it out after 18 hours of growth, transfer it to a high-speed centrifuge at 8000r/min for 10 minutes, and then pour Remove the supernatant of the centrifuge tube, and the precipitate in the lower layer of the centrifuge tube is the MoS 2 /RGO product. The MoS 2 /RGO product is washed three times with deionized water, and dried in a vacuum oven at 100°C for 1 hour to obtain the MoS 2 /RGO composite carrier.
步骤三、Pt-MoS2/RGO催化剂的制备:Step 3. Preparation of Pt-MoS 2 /RGO catalyst:
(1)将0.0200gMoS2/RGO复合载体置于烧杯中,加入60mL去离子水,用超声波清洗机超声处理10min使MoS2/RGO全部溶解,得到混合溶液F。(1) Put 0.0200g of MoS 2 /RGO composite carrier in a beaker, add 60mL of deionized water, and use an ultrasonic cleaner to sonicate for 10 minutes to completely dissolve the MoS 2 /RGO, and obtain a mixed solution F.
(2)将0.0020g H2PtCl6·6H2O加入60mL混合溶液F中并搅拌均匀,然后在20℃下用滴管向其中逐滴滴加60mL 0.5mol/L硼氢化钠溶液,滴加的同时用玻璃棒搅拌均匀,得到反应后的混合物转移至8000r/min的高速离心机中离心10min,倒掉离心管上层清液,离心管下层物质即为Pt-MoS2/RGO催化剂;将Pt-MoS2/RGO催化剂分别用去离子水和质量分数为10%的无水乙醇洗涤三次后置于160℃真空干燥箱中干燥2h,得到纯净的Pt-MoS2/RGO催化剂。(2) Add 0.0020g H 2 PtCl 6 ·6H 2 O into 60mL mixed solution F and stir evenly, then add 60mL 0.5mol/L sodium borohydride solution dropwise with a dropper at 20°C, dropwise add While stirring evenly with a glass rod, the obtained reaction mixture was transferred to an 8000r/min high-speed centrifuge for 10 minutes, and the supernatant of the centrifuge tube was discarded, and the lower layer of the centrifuge tube was the Pt-MoS 2 /RGO catalyst; the Pt -The MoS 2 /RGO catalyst was washed three times with deionized water and 10% absolute ethanol, and then dried in a vacuum oven at 160°C for 2 hours to obtain a pure Pt-MoS 2 /RGO catalyst.
Pt-MoS2/RGO催化剂的活性评价:Activity evaluation of Pt-MoS 2 /RGO catalyst:
催化剂活性测定在高温高压活性测试装置中进行,取催化剂2mg置于反应的等温区范围内。将催化剂在反应装置中于300℃活化2h,然后在测试条件下稳定2h。测定条件为:温度250℃,压力5MPa,反应气N2:H2为1:3(体积比),空速15000h-1。用化学吸收法测得出口反应气中的氨浓度为131.4mmol gcat -1h-1,该原子级活性位点催化剂的催化合成氨活性在54h内没有明显下降。说明本发明所制备的原子级活性位点合成氨催化剂在温和条件下催化活性和稳定性较好。Catalyst activity measurement was carried out in a high temperature and high pressure activity testing device, and 2 mg of catalyst was taken and placed within the range of the isothermal zone of the reaction. The catalyst was activated at 300° C. for 2 h in the reaction apparatus, and then stabilized under the test conditions for 2 h. The measurement conditions are: temperature 250°C, pressure 5MPa, reaction gas N 2 : H 2 ratio 1:3 (volume ratio), space velocity 15000h -1 . The ammonia concentration in the outlet reaction gas was measured by chemical absorption method to be 131.4mmol g cat -1 h -1 , and the ammonia synthesis activity of the atomic-level active site catalyst did not decrease significantly within 54 hours. It shows that the atomic-level active site ammonia synthesis catalyst prepared by the present invention has better catalytic activity and stability under mild conditions.
实施例2Example 2
步骤一、还原氧化石墨烯载体的制备:Step 1, preparation of reduced graphene oxide carrier:
(1)在2℃冰水浴条件下,将60mL质量分数为98%的浓硫酸在玻璃棒搅拌下缓慢加入圆底烧瓶中,随后缓慢加入1.5000g NaNO3和1.5000g石墨粉形成混合溶液;当混合溶液温度降至2℃后,分三次缓慢加入9.0000g高锰酸钾,待最后一次加入高锰酸钾后在2℃冰水浴中恒温反应30min,氧化石墨粉形成硫酸-石墨层间化合物,此时得到的混合溶液记为混合溶液A;撤除冰水浴使混合溶液A温度上升至22℃后继续反应1.5h,深度氧化硫酸-石墨层间化合物,此时得到的混合溶液记为混合溶液B。(1) under 2 ℃ of ice-water bath conditions, the concentrated sulfuric acid that 60mL mass fraction is 98% is slowly added in the round-bottomed flask under glass rod stirring, then slowly add 1.5000g NaNO 3 and 1.5000g graphite powder form mixed solution; After the temperature of the mixed solution drops to 2°C, slowly add 9.0000g of potassium permanganate three times. After the last addition of potassium permanganate, react at a constant temperature in an ice-water bath at 2°C for 30 minutes. The graphite oxide powder forms a sulfuric acid-graphite interlayer compound. The mixed solution obtained at this time is designated as mixed solution A; remove the ice-water bath to raise the temperature of mixed solution A to 22°C and continue the reaction for 1.5 hours to deeply oxidize the sulfuric acid-graphite interlayer compound. The mixed solution obtained at this time is designated as mixed solution B .
(2)将70mL去离子水加入混合溶液B中,利用步骤(1)中加入的残余浓硫酸与水作用时放出的热量使混合溶液B的温度逐渐升至98℃,然后在玻璃棒搅拌下反应0.5h,使混合溶液B中的硫酸-石墨层间化合物发生水解反应。向水解后的混合溶液中加入10mL质量分数为15%的H2O2溶液,除去过量的高锰酸钾,得到的溶液记为混合溶液C;然后将混合溶液C转移至10000r/min的高速离心机中离心20min,倒掉离心管上层清液,离心管下层沉淀物即为氧化石墨烯。(2) Add 70mL deionized water to the mixed solution B, use the heat released when the residual concentrated sulfuric acid added in step (1) reacts with water to gradually raise the temperature of the mixed solution B to 98°C, and then stir it with a glass rod React for 0.5h to make the sulfuric acid-graphite intercalation compound in the mixed solution B undergo a hydrolysis reaction. Add 10 mL of H2O2 solution with a mass fraction of 15% to the mixed solution after hydrolysis, remove excess potassium permanganate, and record the obtained solution as mixed solution C; then transfer mixed solution C to a high-speed Centrifuge in a centrifuge for 20 minutes, pour off the supernatant of the centrifuge tube, and the sediment in the lower layer of the centrifuge tube is graphene oxide.
(3)将离心管下层的氧化石墨烯移至烧杯中,依次向烧杯中加入70mL去离子水、45mL纯净的水合肼,并用玻璃棒搅拌均匀得到混合溶液D;将混合溶液D置于120℃真空干燥箱中反应9h,得到RGO(还原氧化石墨烯)载体,将RGO载体用去离子水洗涤三次,除去残余的水合肼后再次放入真空干燥箱中,于120℃下干燥2h,得到纯净的RGO载体。(3) Move the graphene oxide in the lower layer of the centrifuge tube to a beaker, add 70mL deionized water and 45mL pure hydrazine hydrate to the beaker in turn, and stir with a glass rod to obtain a mixed solution D; put the mixed solution D at 120°C React in a vacuum drying oven for 9 hours to obtain an RGO (reduced graphene oxide) carrier, wash the RGO carrier three times with deionized water, remove the residual hydrazine hydrate, put it in a vacuum drying oven again, and dry it at 120°C for 2 hours to obtain pure The RGO vector.
步骤二、MoS2/RGO复合载体的制备:Step 2. Preparation of MoS 2 /RGO composite carrier:
(1)将0.0036g纯净的RGO载体置于烧杯中,加入70mL去离子水,用超声波清洗机超声处理20min使纯净的RGO全部溶解,得到RGO混合溶液。(1) Put 0.0036 g of pure RGO carrier into a beaker, add 70 mL of deionized water, and use an ultrasonic cleaner to sonicate for 20 min to completely dissolve the pure RGO to obtain a mixed solution of RGO.
(2)将0.0242g钼酸钠加入RGO溶液中并用玻璃棒搅拌均匀得到溶有钼酸钠的RGO混合溶液;将硫脲0.0152g溶于50mL去离子水中得到硫脲溶液;用滴管将该硫脲溶液缓慢滴入溶有钼酸钠的RGO混合溶液中,用玻璃棒搅拌均匀后加入质量分数为10%的盐酸溶液调节pH值为3,得到混合溶液E。(2) Add 0.0242g sodium molybdate in the RGO solution and stir with a glass rod to obtain a RGO mixed solution that is dissolved in sodium molybdate; dissolve 0.0152g of thiourea in 50mL deionized water to obtain a thiourea solution; The thiourea solution was slowly dropped into the RGO mixed solution dissolved in sodium molybdate, stirred evenly with a glass rod, and then 10% hydrochloric acid solution was added to adjust the pH value to 3 to obtain the mixed solution E.
(3)将混合溶液E转移至聚四氟乙烯内衬的不锈钢反应釜中,在150℃条件下生长MoS2,生长24h后取出,转移至10000r/min的高速离心机中离心20min,然后倒掉离心管上层清液,离心管下层沉淀物即为MoS2/RGO,将MoS2/RGO产物用去离子水洗涤三次,置于120℃真空干燥箱中干燥1.5h,得到MoS2/RGO复合载体。(3) Transfer the mixed solution E to a polytetrafluoroethylene-lined stainless steel reactor, grow MoS 2 at 150°C, take it out after 24 hours of growth, transfer it to a high-speed centrifuge at 10,000 r/min for 20 minutes, and then pour Remove the supernatant from the centrifuge tube, and the precipitate in the lower layer of the centrifuge tube is MoS 2 /RGO. Wash the MoS 2 /RGO product three times with deionized water, and dry it in a vacuum oven at 120°C for 1.5 hours to obtain the MoS 2 /RGO composite carrier.
步骤三、Pt-MoS2/RGO催化剂的制备:Step 3. Preparation of Pt-MoS 2 /RGO catalyst:
(1)将0.0400gMoS2/RGO复合载体置于烧杯中,加入70mL去离子水,用超声波清洗机超声处理20min使MoS2/RGO全部溶解,得到混合溶液F。(1) Put 0.0400g of MoS 2 /RGO composite carrier in a beaker, add 70mL of deionized water, and use an ultrasonic cleaner to sonicate for 20 minutes to completely dissolve the MoS 2 /RGO, and obtain a mixed solution F.
(2)将0.0040g H2PtCl6·6H2O加入70mL混合溶液F中并搅拌均匀,然后在22℃下用滴管向其中逐滴滴加70mL 0.5mol/L硼氢化钠溶液,滴加的同时用玻璃棒搅拌均匀,得到反应后的混合物转移至10000r/min的高速离心机中离心20min,倒掉离心管上层清液,离心管下层物质即为Pt-MoS2/RGO催化剂;将Pt-MoS2/RGO催化剂分别用去离子水和质量分数为20%的无水乙醇洗涤三次后置于180℃真空干燥箱中干燥3h,得到纯净的Pt-MoS2/RGO催化剂。(2) Add 0.0040g H 2 PtCl 6 ·6H 2 O into 70mL mixed solution F and stir evenly, then add 70mL 0.5mol/L sodium borohydride solution dropwise with a dropper at 22°C, dropwise add While stirring evenly with a glass rod, the obtained reacted mixture was transferred to a high-speed centrifuge at 10,000r/min for 20 minutes, and the supernatant of the centrifuge tube was discarded, and the lower layer of the centrifuge tube was the Pt-MoS 2 /RGO catalyst; the Pt -The MoS 2 /RGO catalyst was washed three times with deionized water and 20% absolute ethanol respectively, and then dried in a vacuum oven at 180°C for 3 hours to obtain a pure Pt-MoS 2 /RGO catalyst.
Pt-MoS2/RGO催化剂的活性评价:Activity evaluation of Pt-MoS 2 /RGO catalyst:
催化剂活性测定在高温高压活性测试装置中进行,取催化剂2mg置于反应的等温区范围内。将催化剂在反应装置中于300℃活化2h,然后在测试条件下稳定2h。测定条件为:温度250℃,压力5MPa,反应气N2:H2为1:3(体积比),空速15000h-1。用化学吸收法测得出口反应气中的氨浓度为742.6mmol gcat -1h-1,该原子级活性位点催化剂的催化合成氨活性在54h内没有明显下降。说明本发明所制备的原子级活性位点合成氨催化剂在温和条件下催化活性和稳定性较好。Catalyst activity measurement was carried out in a high temperature and high pressure activity testing device, and 2 mg of catalyst was taken and placed within the range of the isothermal zone of the reaction. The catalyst was activated at 300° C. for 2 h in the reaction apparatus, and then stabilized under the test conditions for 2 h. The measurement conditions are: temperature 250°C, pressure 5MPa, reaction gas N 2 : H 2 ratio 1:3 (volume ratio), space velocity 15000h -1 . The ammonia concentration in the outlet reaction gas was measured by chemical absorption method to be 742.6mmol g cat -1 h -1 , and the catalytic activity of the atomic-level active site catalyst for ammonia synthesis did not decrease significantly within 54 hours. It shows that the atomic-level active site ammonia synthesis catalyst prepared by the present invention has better catalytic activity and stability under mild conditions.
实施例3Example 3
步骤一、还原氧化石墨烯载体的制备:Step 1, preparation of reduced graphene oxide carrier:
(1)在3℃冰水浴条件下,将90mL质量分数为98%的浓硫酸在玻璃棒搅拌下缓慢加入圆底烧瓶中,随后缓慢加入1.8000g NaNO3和1.8000g石墨粉形成混合溶液;当混合溶液温度降至3℃后,分三次缓慢加入10.0000g高锰酸钾,待最后一次加入高锰酸钾后在3℃冰水浴中恒温反应35min,氧化石墨粉形成硫酸-石墨层间化合物,此时得到的混合溶液记为混合溶液A;撤除冰水浴使混合溶液A温度上升至24℃后继续反应2.5h,深度氧化硫酸-石墨层间化合物,此时得到的混合溶液记为混合溶液B。(1) under 3 ℃ of ice-water bath conditions, the concentrated sulfuric acid that 90mL mass fraction is 98% is slowly added in the round-bottomed flask under glass rod stirring, then slowly adds 1.8000g NaNO 3 and 1.8000g graphite powder form mixed solution; After the temperature of the mixed solution is lowered to 3°C, slowly add 10.0000g of potassium permanganate three times. After adding potassium permanganate for the last time, react at a constant temperature in an ice-water bath at 3°C for 35 minutes. The graphite oxide powder forms a sulfuric acid-graphite interlayer compound. The mixed solution obtained at this time is designated as mixed solution A; remove the ice-water bath to raise the temperature of mixed solution A to 24°C and continue to react for 2.5 hours to deeply oxidize the sulfuric acid-graphite interlayer compound. The mixed solution obtained at this time is designated as mixed solution B .
(2)将90mL去离子水加入混合溶液B中,利用步骤(1)中加入的残余的浓硫酸与水作用时放出的热量使混合溶液B的温度逐渐升至99℃,然后在玻璃棒搅拌下反应0.6h,使混合溶液B中的硫酸-石墨层间化合物发生水解反应。向水解后的混合溶液中加入20mL质量分数为28%的H2O2溶液,除去过量的高锰酸钾,得到的溶液记为混合溶液C;然后将混合溶液C转移至11000r/min的高速离心机中离心30min,倒掉离心管上层清液,离心管下层沉淀物即为氧化石墨烯。(2) Add 90mL deionized water into the mixed solution B, use the heat released when the residual concentrated sulfuric acid added in step (1) interacts with water to gradually raise the temperature of the mixed solution B to 99°C, and then stir with a glass rod The reaction was carried out for 0.6h, so that the sulfuric acid-graphite intercalation compound in the mixed solution B was hydrolyzed. Add 20mL of H2O2 solution with a mass fraction of 28% to the mixed solution after hydrolysis, remove excess potassium permanganate, and record the obtained solution as mixed solution C; then transfer mixed solution C to a high-speed 11000r/min Centrifuge in a centrifuge for 30 minutes, pour off the supernatant of the centrifuge tube, and the sediment in the lower layer of the centrifuge tube is graphene oxide.
(3)将离心管下层的氧化石墨烯移至烧杯中,依次向烧杯中加入90mL去离子水、50mL纯净的水合肼,并用玻璃棒搅拌均匀得到混合溶液D;将混合溶液D置于130℃真空干燥箱中反应9.5h,得到RGO(还原氧化石墨烯)载体,将RGO载体用去离子水洗涤三次,除去残余的水合肼后再次放入真空干燥箱中,于130℃下干燥2.5h,得到纯净的RGO载体。(3) Move the graphene oxide in the lower layer of the centrifuge tube to a beaker, add 90mL deionized water and 50mL pure hydrazine hydrate to the beaker in turn, and stir with a glass rod to obtain a mixed solution D; put the mixed solution D at 130°C React in a vacuum drying oven for 9.5 hours to obtain an RGO (reduced graphene oxide) carrier, wash the RGO carrier three times with deionized water, remove the residual hydrazine hydrate, put it in a vacuum drying oven again, and dry it at 130°C for 2.5 hours. Obtain pure RGO carrier.
步骤二、MoS2/RGO复合载体的制备:Step 2. Preparation of MoS 2 /RGO composite carrier:
(1)将0.0040g纯净的RGO载体置于烧杯中,加入90mL去离子水,用超声波清洗机超声处理28min使纯净的RGO全部溶解,得到RGO混合溶液。(1) Put 0.0040 g of pure RGO carrier in a beaker, add 90 mL of deionized water, and use an ultrasonic cleaner to sonicate for 28 min to completely dissolve the pure RGO to obtain a mixed solution of RGO.
(2)将0.0242g钼酸钠加入RGO溶液中并用玻璃棒搅拌均匀得到溶有钼酸钠的RGO混合溶液;将硫脲0.0290g溶于58mL去离子水中得到硫脲溶液;用滴管将该硫脲溶液缓慢滴入溶有钼酸钠的RGO混合溶液中,用玻璃棒搅拌均匀后加入质量分数为10%的盐酸溶液调节pH值为5,得到混合溶液E。(2) Add 0.0242g of sodium molybdate into the RGO solution and stir with a glass rod to obtain a RGO mixed solution of sodium molybdate; dissolve 0.0290g of thiourea in 58mL of deionized water to obtain a thiourea solution; The thiourea solution was slowly dropped into the RGO mixed solution dissolved in sodium molybdate, stirred evenly with a glass rod, and then 10% hydrochloric acid solution was added to adjust the pH value to 5 to obtain the mixed solution E.
(3)将混合溶液E转移至聚四氟乙烯内衬的不锈钢反应釜中,在220℃条件下生长MoS2,生长26h后取出,转移至11000r/min的高速离心机中离心35min,然后倒掉离心管上层清液,离心管下层沉淀物即为MoS2/RGO产物,将MoS2/RGO产物用去离子水洗涤三次,置于130℃真空干燥箱中干燥2.5h,得到MoS2/RGO复合载体。(3) Transfer the mixed solution E to a polytetrafluoroethylene-lined stainless steel reactor, grow MoS 2 at 220°C, take it out after 26 hours of growth, transfer it to a high-speed centrifuge at 11,000 r/min for 35 minutes, and then pour Remove the supernatant of the centrifuge tube, and the precipitate in the lower layer of the centrifuge tube is the MoS 2 /RGO product. The MoS 2 /RGO product is washed three times with deionized water, and dried in a vacuum oven at 130°C for 2.5 hours to obtain MoS 2 /RGO Composite carrier.
步骤三、Pt-MoS2/RGO催化剂的制备:Step 3. Preparation of Pt-MoS 2 /RGO catalyst:
(1)将0.0600gMoS2/RGO复合载体置于烧杯中,加入90mL去离子水,用超声波清洗机超声处理28min使MoS2/RGO全部溶解,得到混合溶液F。(1) Put 0.0600g of MoS 2 /RGO composite carrier in a beaker, add 90mL of deionized water, and use an ultrasonic cleaner to sonicate for 28 minutes to completely dissolve the MoS 2 /RGO, and obtain a mixed solution F.
(2)将0.0080g H2PtCl6·6H2O加入90mL混合溶液F中并搅拌均匀,然后在24℃下用滴管向其中逐滴滴加90mL 0.5mol/L硼氢化钠溶液,滴加的同时用玻璃棒搅拌均匀,得到反应后的混合物转移至11000r/min的高速离心机中离心35min,倒掉离心管上层清液,离心管下层物质即为Pt-MoS2/RGO催化剂;将Pt-MoS2/RGO催化剂分别用去离子水和质量分数为28%的无水乙醇洗涤三次后置于220℃真空干燥箱中干燥4h,得到纯净的Pt-MoS2/RGO催化剂。(2) Add 0.0080g H 2 PtCl 6 ·6H 2 O into 90mL mixed solution F and stir evenly, then add 90mL 0.5mol/L sodium borohydride solution dropwise with a dropper at 24°C, dropwise add While stirring evenly with a glass rod, the obtained reacted mixture was transferred to a high-speed centrifuge at 11000r/min for 35 minutes, and the supernatant of the centrifuge tube was discarded, and the lower layer of the centrifuge tube was the Pt-MoS 2 /RGO catalyst; the Pt - The MoS 2 /RGO catalyst was washed three times with deionized water and 28% absolute ethanol, and then dried in a vacuum oven at 220°C for 4 hours to obtain a pure Pt-MoS 2 /RGO catalyst.
Pt-MoS2/RGO催化剂的活性评价:Activity evaluation of Pt-MoS 2 /RGO catalyst:
催化剂活性测定在高温高压活性测试装置中进行,取催化剂2mg置于反应的等温区范围内。将催化剂在反应装置中于300℃活化2h,然后在测试条件下稳定2h。测定条件为:温度250℃,压力5MPa,反应气N2:H2为1:3(体积比),空速15000h-1。用化学吸收法测得出口反应气中的氨浓度为631.2mmol gcat -1h-1,该原子级活性位点催化剂的催化合成氨活性在54h内没有明显下降。说明本发明所制备的原子级活性位点合成氨催化剂在温和条件下催化活性和稳定性较好。Catalyst activity measurement was carried out in a high temperature and high pressure activity testing device, and 2 mg of catalyst was taken and placed within the range of the isothermal zone of the reaction. The catalyst was activated at 300° C. for 2 h in the reaction apparatus, and then stabilized under the test conditions for 2 h. The measurement conditions are: temperature 250°C, pressure 5MPa, reaction gas N 2 : H 2 ratio 1:3 (volume ratio), space velocity 15000h -1 . The ammonia concentration in the outlet reaction gas was measured by chemical absorption method to be 631.2mmol g cat -1 h -1 , and the catalytic activity of the atomic-level active site catalyst for ammonia synthesis did not decrease significantly within 54 hours. It shows that the atomic-level active site ammonia synthesis catalyst prepared by the present invention has better catalytic activity and stability under mild conditions.
实施例4Example 4
步骤一、还原氧化石墨烯载体的制备:Step 1, preparation of reduced graphene oxide carrier:
(1)在4℃冰水浴条件下,将100mL质量分数为98%的浓硫酸在玻璃棒搅拌下缓慢加入圆底烧瓶中,随后缓慢加入2.0000g NaNO3和2.0000g石墨粉形成混合溶液;当混合溶液温度降至4℃后,分三次缓慢加入12.0000g高锰酸钾,待最后一次加入高锰酸钾后在4℃冰水浴中恒温反应40min,氧化石墨粉形成硫酸-石墨层间化合物,此时得到的混合溶液记为混合溶液A;撤除冰水浴使混合溶液A温度上升至25℃后继续反应3h,深度氧化硫酸-石墨层间化合物,此时得到的混合溶液记为混合溶液B。(1) under 4 ℃ of ice-water bath conditions, the concentrated sulfuric acid that 100mL mass fraction is 98% is slowly added in the round-bottomed flask under glass rod stirring, then slowly add 2.0000g NaNO 3 and 2.0000g graphite powder form mixed solution; After the temperature of the mixed solution is lowered to 4°C, slowly add 12.0000g of potassium permanganate three times. After adding potassium permanganate for the last time, react at a constant temperature in an ice-water bath at 4°C for 40 minutes. The graphite oxide powder forms a sulfuric acid-graphite interlayer compound. The mixed solution obtained at this time was designated as mixed solution A; the ice-water bath was removed to raise the temperature of mixed solution A to 25°C, and then the reaction was continued for 3 hours to deeply oxidize the sulfuric acid-graphite intercalation compound. The mixed solution obtained at this time was designated as mixed solution B.
(2)将100mL去离子水加入混合溶液B中,利用步骤(1)中加入的残余浓硫酸与水作用时放出的热量使混合溶液B的温度逐渐升至100℃,然后在玻璃棒搅拌下反应0.7h,使混合溶液B中的硫酸-石墨层间化合物发生水解反应。向水解后的混合溶液中加入25mL质量分数为30%的H2O2溶液,除去过量的高锰酸钾,得到的溶液记为混合溶液C;然后将混合溶液C转移至12000r/min的高速离心机中离心40min,倒掉离心管上层清液,离心管下层沉淀物即为氧化石墨烯。(2) Add 100mL deionized water to the mixed solution B, use the heat released when the residual concentrated sulfuric acid added in step (1) interacts with water to gradually raise the temperature of the mixed solution B to 100°C, and then stir it with a glass rod After reacting for 0.7h, the sulfuric acid-graphite intercalation compound in the mixed solution B undergoes a hydrolysis reaction. Add 25mL of H2O2 solution with a mass fraction of 30% to the mixed solution after hydrolysis, remove excess potassium permanganate, and record the obtained solution as mixed solution C ; then transfer mixed solution C to a high-speed 12000r/min Centrifuge in a centrifuge for 40 minutes, pour off the supernatant of the centrifuge tube, and the sediment in the lower layer of the centrifuge tube is graphene oxide.
(3)将离心管下层的氧化石墨烯移至烧杯中,依次向烧杯中加入100mL去离子水、60mL纯净的水合肼,并用玻璃棒搅拌均匀得到混合溶液D;将混合溶液D置于140℃真空干燥箱中反应10h,得到RGO(还原氧化石墨烯)载体,将RGO载体用去离子水洗涤三次,除去残余的水合肼后再次放入真空干燥箱中,于140℃下干燥3h,得到纯净的RGO载体。(3) Move the graphene oxide in the lower layer of the centrifuge tube to a beaker, add 100mL deionized water and 60mL pure hydrazine hydrate to the beaker in turn, and stir with a glass rod to obtain a mixed solution D; put the mixed solution D at 140°C React in a vacuum drying oven for 10 hours to obtain an RGO (reduced graphene oxide) carrier, wash the RGO carrier three times with deionized water, remove the residual hydrazine hydrate, put it in a vacuum drying oven again, and dry it at 140°C for 3 hours to obtain pure The RGO vector.
步骤二、MoS2/RGO复合载体的制备:Step 2. Preparation of MoS 2 /RGO composite carrier:
(1)将0.0048g纯净的RGO载体置于烧杯中,加入100mL去离子水,用超声波清洗机超声处理30min使纯净的RGO全部溶解,得到RGO混合溶液。(1) Put 0.0048 g of pure RGO carrier in a beaker, add 100 mL of deionized water, and use an ultrasonic cleaner to sonicate for 30 min to completely dissolve the pure RGO to obtain a mixed solution of RGO.
(2)将0.0242g钼酸钠加入RGO溶液中并用玻璃棒搅拌均匀得到溶有钼酸钠的RGO混合溶液;将硫脲0.0380g溶于60mL去离子水中得到硫脲溶液,用滴管将该硫脲溶液缓慢滴入溶有钼酸钠的RGO混合溶液中,用玻璃棒搅拌均匀后加入质量分数为10%的盐酸溶液调节pH值为7,得到混合溶液E。(2) Add 0.0242g of sodium molybdate into the RGO solution and stir evenly with a glass rod to obtain a mixed solution of RGO having sodium molybdate; dissolve 0.0380g of thiourea in 60mL of deionized water to obtain a thiourea solution, and use a The thiourea solution was slowly dropped into the RGO mixed solution dissolved in sodium molybdate, stirred evenly with a glass rod, and then 10% hydrochloric acid solution was added to adjust the pH value to 7 to obtain the mixed solution E.
(3)将混合溶液E转移至聚四氟乙烯内衬的不锈钢反应釜中,在250℃条件下生长MoS2,生长30h后取出,转移至12000r/min的高速离心机中离心40min,然后倒掉离心管上层清液,离心管下层沉淀物即为MoS2/RGO产物,将MoS2/RGO产物用去离子水洗涤三次,置于140℃真空干燥箱中干燥3h,得到MoS2/RGO复合载体。(3) Transfer the mixed solution E to a polytetrafluoroethylene-lined stainless steel reactor, grow MoS 2 at 250°C, take it out after 30 hours of growth, transfer it to a high-speed centrifuge at 12,000 r/min for 40 minutes, and then pour Remove the supernatant of the centrifuge tube, and the precipitate in the lower layer of the centrifuge tube is the MoS 2 /RGO product. The MoS 2 /RGO product is washed three times with deionized water, and dried in a vacuum oven at 140°C for 3 hours to obtain the MoS 2 /RGO composite carrier.
步骤三、Pt-MoS2/RGO催化剂的制备:Step 3. Preparation of Pt-MoS 2 /RGO catalyst:
(1)将0.0800gMoS2/RGO复合载体置于烧杯中,加入100mL去离子水,用超声波清洗机超声处理30min使MoS2/RGO全部溶解,得到混合溶液F。(1) Put 0.0800g of MoS 2 /RGO composite carrier in a beaker, add 100mL of deionized water, and use an ultrasonic cleaner to sonicate for 30 minutes to completely dissolve the MoS 2 /RGO, and obtain a mixed solution F.
(2)将0.0100g H2PtCl6·6H2O加入100mL混合溶液F中并搅拌均匀,然后在25℃下用滴管向其中逐滴滴加100mL 0.5mol/L硼氢化钠溶液,滴加的同时用玻璃棒搅拌均匀,得到反应后的混合物转移至12000r/min的高速离心机中离心40min,倒掉离心管上层清液,离心管下层物质即为Pt-MoS2/RGO催化剂;将Pt-MoS2/RGO催化剂分别用去离子水和质量分数为30%的无水乙醇洗涤三次后置于240℃真空干燥箱中干燥5h,得到纯净的Pt-MoS2/RGO催化剂。(2) Add 0.0100g H 2 PtCl 6 ·6H 2 O into 100mL mixed solution F and stir evenly, then add 100mL 0.5mol/L sodium borohydride solution dropwise with a dropper at 25°C, dropwise While stirring evenly with a glass rod, the obtained reaction mixture was transferred to a high-speed centrifuge at 12000r/min for 40 minutes, and the supernatant of the centrifuge tube was discarded, and the lower layer of the centrifuge tube was the Pt-MoS 2 /RGO catalyst; the Pt -The MoS 2 /RGO catalyst was washed three times with deionized water and 30% absolute ethanol, and then dried in a vacuum oven at 240°C for 5 hours to obtain a pure Pt-MoS 2 /RGO catalyst.
Pt-MoS2/RGO催化剂的活性评价:Activity evaluation of Pt-MoS 2 /RGO catalyst:
催化剂活性测定在高温高压活性测试装置中进行,取催化剂2mg置于反应的等温区范围内。将催化剂在反应装置中于300℃活化2h,然后在测试条件下稳定2h。测定条件为:温度250℃,压力5MPa,反应气N2:H2为1:3(体积比),空速15000h-1。用化学吸收法测得出口反应气中的氨浓度为398.1mmol gcat -1h-1,该原子级活性位点催化剂的催化合成氨活性在54h内没有明显下降。说明本发明所制备的原子级活性位点合成氨催化剂在温和条件下催化活性和稳定性较好。Catalyst activity measurement was carried out in a high temperature and high pressure activity testing device, and 2 mg of catalyst was taken and placed within the range of the isothermal zone of the reaction. The catalyst was activated at 300° C. for 2 h in the reaction apparatus, and then stabilized under the test conditions for 2 h. The measurement conditions are: temperature 250°C, pressure 5MPa, reaction gas N 2 : H 2 ratio 1:3 (volume ratio), space velocity 15000h -1 . The ammonia concentration in the outlet reaction gas was measured by chemical absorption method to be 398.1mmol g cat -1 h -1 , and the catalytic activity of the atomic-level active site catalyst for ammonia synthesis did not decrease significantly within 54 hours. It shows that the atomic-level active site ammonia synthesis catalyst prepared by the present invention has better catalytic activity and stability under mild conditions.
从以上4个实施例可知,本发明制备的温和条件下原子级活性位点合成氨催化剂Pt-MoS2/RGO性能优异,具有较高的合成氨活性和稳定性。From the above four examples, it can be seen that the catalyst Pt-MoS 2 /RGO prepared by the present invention for ammonia synthesis with atomic active sites under mild conditions has excellent performance, and has high ammonia synthesis activity and stability.
提供以上实施例仅是为了描述本发明的目的,而并非要限制本发明的范围。在不超出本发明的主旨范围内,对实验条件及方法进行灵活的变更,这些都属于本发明的保护范围,本发明的范围由所附权利要求限定。The above embodiments are provided only for the purpose of describing the present invention, not to limit the scope of the present invention. Within the scope of the gist of the present invention, flexible changes to the experimental conditions and methods all belong to the protection scope of the present invention, and the scope of the present invention is defined by the appended claims.
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