CN109382125B - Nickel-nitrogen co-doped carbon-based electrocatalyst and preparation method and application thereof - Google Patents
Nickel-nitrogen co-doped carbon-based electrocatalyst and preparation method and application thereof Download PDFInfo
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- 239000010411 electrocatalyst Substances 0.000 title claims abstract description 57
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 title claims abstract description 46
- 229910052799 carbon Inorganic materials 0.000 title claims abstract description 42
- HZUJFPFEXQTAEL-UHFFFAOYSA-N azanylidynenickel Chemical compound [N].[Ni] HZUJFPFEXQTAEL-UHFFFAOYSA-N 0.000 title claims abstract description 35
- 238000002360 preparation method Methods 0.000 title claims abstract description 19
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 claims abstract description 50
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 36
- NLXLAEXVIDQMFP-UHFFFAOYSA-N Ammonia chloride Chemical compound [NH4+].[Cl-] NLXLAEXVIDQMFP-UHFFFAOYSA-N 0.000 claims abstract description 34
- 238000001354 calcination Methods 0.000 claims abstract description 32
- 229910002092 carbon dioxide Inorganic materials 0.000 claims abstract description 25
- 238000001027 hydrothermal synthesis Methods 0.000 claims abstract description 22
- PXHVJJICTQNCMI-UHFFFAOYSA-N Nickel Chemical compound [Ni] PXHVJJICTQNCMI-UHFFFAOYSA-N 0.000 claims abstract description 19
- 150000002815 nickel Chemical class 0.000 claims abstract description 19
- WQZGKKKJIJFFOK-GASJEMHNSA-N Glucose Natural products OC[C@H]1OC(O)[C@H](O)[C@@H](O)[C@@H]1O WQZGKKKJIJFFOK-GASJEMHNSA-N 0.000 claims abstract description 18
- 239000001569 carbon dioxide Substances 0.000 claims abstract description 18
- 239000008103 glucose Substances 0.000 claims abstract description 18
- 235000019270 ammonium chloride Nutrition 0.000 claims abstract description 17
- QGBSISYHAICWAH-UHFFFAOYSA-N dicyandiamide Chemical compound NC(N)=NC#N QGBSISYHAICWAH-UHFFFAOYSA-N 0.000 claims abstract description 17
- 238000006243 chemical reaction Methods 0.000 claims abstract description 10
- 238000000034 method Methods 0.000 claims abstract description 8
- 229910052759 nickel Inorganic materials 0.000 claims abstract description 8
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- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 claims description 11
- 239000012300 argon atmosphere Substances 0.000 claims description 9
- 229910052757 nitrogen Inorganic materials 0.000 claims description 7
- 230000001603 reducing effect Effects 0.000 claims description 3
- 230000009467 reduction Effects 0.000 abstract description 13
- 239000003054 catalyst Substances 0.000 abstract description 11
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 abstract description 5
- 229910002091 carbon monoxide Inorganic materials 0.000 abstract description 5
- 238000005054 agglomeration Methods 0.000 abstract description 3
- 230000002776 aggregation Effects 0.000 abstract description 3
- 239000003575 carbonaceous material Substances 0.000 abstract description 3
- 238000009776 industrial production Methods 0.000 abstract description 3
- 230000008569 process Effects 0.000 abstract description 3
- 238000010586 diagram Methods 0.000 description 18
- 230000000052 comparative effect Effects 0.000 description 17
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 14
- 238000001816 cooling Methods 0.000 description 14
- 238000010438 heat treatment Methods 0.000 description 14
- 238000006722 reduction reaction Methods 0.000 description 14
- 238000004832 voltammetry Methods 0.000 description 10
- 238000003756 stirring Methods 0.000 description 8
- 229910021586 Nickel(II) chloride Inorganic materials 0.000 description 7
- 239000008367 deionised water Substances 0.000 description 7
- 229910021641 deionized water Inorganic materials 0.000 description 7
- QMMRZOWCJAIUJA-UHFFFAOYSA-L nickel dichloride Chemical compound Cl[Ni]Cl QMMRZOWCJAIUJA-UHFFFAOYSA-L 0.000 description 7
- 239000010453 quartz Substances 0.000 description 7
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N silicon dioxide Inorganic materials O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 7
- 239000011159 matrix material Substances 0.000 description 5
- 229910021389 graphene Inorganic materials 0.000 description 4
- 241000282414 Homo sapiens Species 0.000 description 3
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- 238000003917 TEM image Methods 0.000 description 2
- 238000002441 X-ray diffraction Methods 0.000 description 2
- 238000000026 X-ray photoelectron spectrum Methods 0.000 description 2
- DLGYNVMUCSTYDQ-UHFFFAOYSA-N azane;pyridine Chemical compound N.C1=CC=NC=C1 DLGYNVMUCSTYDQ-UHFFFAOYSA-N 0.000 description 2
- 238000010531 catalytic reduction reaction Methods 0.000 description 2
- 239000003208 petroleum Substances 0.000 description 2
- 230000004083 survival effect Effects 0.000 description 2
- 238000001075 voltammogram Methods 0.000 description 2
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 1
- 238000009825 accumulation Methods 0.000 description 1
- MQRWBMAEBQOWAF-UHFFFAOYSA-N acetic acid;nickel Chemical compound [Ni].CC(O)=O.CC(O)=O MQRWBMAEBQOWAF-UHFFFAOYSA-N 0.000 description 1
- 239000012298 atmosphere Substances 0.000 description 1
- 238000004177 carbon cycle Methods 0.000 description 1
- 238000003763 carbonization Methods 0.000 description 1
- 238000006555 catalytic reaction Methods 0.000 description 1
- 230000001419 dependent effect Effects 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 229910052737 gold Inorganic materials 0.000 description 1
- 238000003837 high-temperature calcination Methods 0.000 description 1
- 239000001257 hydrogen Substances 0.000 description 1
- 229910052739 hydrogen Inorganic materials 0.000 description 1
- 239000010410 layer Substances 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
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- 229940078494 nickel acetate Drugs 0.000 description 1
- KBJMLQFLOWQJNF-UHFFFAOYSA-N nickel(ii) nitrate Chemical compound [Ni+2].[O-][N+]([O-])=O.[O-][N+]([O-])=O KBJMLQFLOWQJNF-UHFFFAOYSA-N 0.000 description 1
- 229910000510 noble metal Inorganic materials 0.000 description 1
- 230000001737 promoting effect Effects 0.000 description 1
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- 229910052709 silver Inorganic materials 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
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- 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
- B01J27/24—Nitrogen compounds
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- B01J37/00—Processes, in general, for preparing catalysts; Processes, in general, for activation of catalysts
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Abstract
Description
技术领域technical field
本发明属于催化技术领域,尤其涉及一种镍氮共掺杂碳基电催化剂、其制备方法及其应用。The invention belongs to the technical field of catalysis, and in particular relates to a nickel-nitrogen co-doped carbon-based electrocatalyst, a preparation method and application thereof.
背景技术Background technique
能源是人类社会生存和发展的基础。目前人类所需的能源严重依赖于石油能源。对石油能源的过度消耗不仅加剧了能源危机,还致使所产生的二氧化碳过度排放,带来了日趋严重的温室效应,严重威胁到人类的生存与发展。对二氧化碳的转化利用不仅能有效的降低大气中二氧化碳的积累,还能将二氧化碳转化成含碳化学品,从而促进碳的循环。Energy is the basis for the survival and development of human society. At present, the energy needed by human beings is heavily dependent on petroleum energy. Excessive consumption of petroleum energy not only aggravates the energy crisis, but also leads to excessive emissions of carbon dioxide, which brings about an increasingly serious greenhouse effect, which seriously threatens the survival and development of human beings. The conversion and utilization of carbon dioxide can not only effectively reduce the accumulation of carbon dioxide in the atmosphere, but also convert carbon dioxide into carbon-containing chemicals, thereby promoting the carbon cycle.
通过电催化对二氧化碳进行还原是目前最具前景的实现二氧化碳转化利用的方式之一。尽管针对二氧化碳电催化还原取得了很多进展,但是还原产物的多样性使得二氧化碳还原选择性低,尤其是水还原至氢气成为二氧化碳催化还原过程中的主要竞争反应,从而导致二氧化碳转化率低下。贵金属比如Au、Ag应用于二氧化碳还原时表现出优异的选择性,但是其昂贵的价格仍然限制了作为二氧化碳还原电催化剂的进一步发展。因此寻找廉价高效的二氧化碳还原电催化剂成为亟待解决的问题。The reduction of carbon dioxide by electrocatalysis is one of the most promising ways to realize the conversion and utilization of carbon dioxide. Although many progresses have been made on the electrocatalytic reduction of CO2, the diversity of reduction products leads to low CO2 reduction selectivity, especially the reduction of water to hydrogen becomes the main competing reaction in the catalytic reduction of CO2, resulting in low CO2 conversion. Noble metals such as Au and Ag show excellent selectivity when applied to CO2 reduction, but their expensive prices still limit their further development as electrocatalysts for CO2 reduction. Therefore, finding cheap and efficient electrocatalysts for CO2 reduction has become an urgent problem.
发明内容SUMMARY OF THE INVENTION
本发明的目的在于提供一种镍氮共掺杂碳基电催化剂、其制备方法及应用,本发明中的镍氮共掺杂碳基电催化剂的反应选择性高,且成本低廉。The purpose of the present invention is to provide a nickel-nitrogen co-doped carbon-based electrocatalyst, a preparation method and application thereof, and the nickel-nitrogen co-doped carbon-based electrocatalyst in the present invention has high reaction selectivity and low cost.
本发明提供一种镍氮共掺杂碳基电催化剂的制备方法,包括以下步骤:The present invention provides a method for preparing a nickel-nitrogen co-doped carbon-based electrocatalyst, comprising the following steps:
A)将镍盐、双氰胺和氯化铵在水中分散,干燥后进行煅烧;A) disperse nickel salt, dicyandiamide and ammonium chloride in water, and calcine after drying;
B)将煅烧后的产品与葡萄糖在水中混合后进行水热反应;B) the product after calcination is mixed with glucose in water to carry out hydrothermal reaction;
C)将水热反应的产品进行煅烧,得到镍氮共掺杂碳基电催化剂。C) calcining the product of the hydrothermal reaction to obtain a nickel-nitrogen co-doped carbon-based electrocatalyst.
优选的,所述镍盐为二价可溶性镍盐。Preferably, the nickel salt is a divalent soluble nickel salt.
优选的,所述镍盐与双氰胺的质量比为(0.2~5):100;Preferably, the mass ratio of the nickel salt to the dicyandiamide is (0.2-5): 100;
所述镍盐与氯化铵的质量比为(0.2~5):500。The mass ratio of the nickel salt to the ammonium chloride is (0.2-5):500.
优选的,所述步骤A)中煅烧的温度为500~650℃;Preferably, the calcination temperature in the step A) is 500-650°C;
所述步骤A)中煅烧的时间为1~4小时。The calcination time in the step A) is 1 to 4 hours.
优选的,所述步骤A)中煅烧后的产品与葡萄糖的质量比为(0.7~1.5):5。Preferably, the mass ratio of the calcined product in the step A) to the glucose is (0.7-1.5):5.
优选的,所述水热反应的温度为160~200℃;Preferably, the temperature of the hydrothermal reaction is 160-200°C;
所述水热反应的时间为10~20小时。The time of the hydrothermal reaction is 10-20 hours.
优选的,所述步骤C)中煅烧的温度为800~1100℃;Preferably, the calcination temperature in the step C) is 800-1100°C;
所述步骤C)中煅烧的时间为0.5~4小时。The calcination time in the step C) is 0.5 to 4 hours.
本发明提供一种镍氮共掺杂碳基电催化剂,按照上述制备方法制得。The present invention provides a nickel-nitrogen co-doped carbon-based electrocatalyst, which is prepared according to the above preparation method.
优选的,所述镍氮共掺杂碳基电催化剂中氮的质量分数为3~6%;Preferably, the mass fraction of nitrogen in the nickel-nitrogen co-doped carbon-based electrocatalyst is 3-6%;
所述镍氮共掺杂碳基电催化剂中镍的质量分数为1~3%。The mass fraction of nickel in the nickel-nitrogen co-doped carbon-based electrocatalyst is 1-3%.
上文所述的镍氮共掺杂碳基电催化剂在还原二氧化碳反应中的应用Application of Ni-nitrogen Co-doped Carbon-Based Electrocatalysts in Carbon Dioxide Reduction Reaction
本发明提供了一种镍氮共掺杂碳基电催化剂的制备方法,包括以下步骤:A)将镍盐、双氰胺和氯化铵在水中分散,干燥后进行煅烧;B)将煅烧后的产品与葡萄糖在水中混合后进行水热反应;C)将水热反应的产品进行煅烧,得到镍氮共掺杂碳基电催化剂。本发明利用限域反应,将单原子形式的镍分散在氮掺杂的碳基材料中,避免了活性位点的团聚和流失。所制得的催化剂表现出优异的电催化二氧化碳还原性能,对一氧化碳的选择性可达99%。本发明提供的制备方法具有工艺流程简单、成本低廉、产量大适合于工业生产等特点,具有潜在的应用价值。The present invention provides a method for preparing a nickel-nitrogen co-doped carbon-based electrocatalyst, comprising the following steps: A) dispersing nickel salt, dicyandiamide and ammonium chloride in water, drying and then calcining; B) calcining After mixing the product with glucose in water, a hydrothermal reaction is carried out; C) the product of the hydrothermal reaction is calcined to obtain a nickel-nitrogen co-doped carbon-based electrocatalyst. The invention utilizes the confinement reaction to disperse nickel in the form of single atoms in the nitrogen-doped carbon-based material, thereby avoiding the agglomeration and loss of active sites. The prepared catalyst exhibits excellent electrocatalytic carbon dioxide reduction performance, and the selectivity to carbon monoxide can reach 99%. The preparation method provided by the invention has the characteristics of simple process flow, low cost, large output, suitable for industrial production and the like, and has potential application value.
附图说明Description of drawings
为了更清楚地说明本发明实施例或现有技术中的技术方案,下面将对实施例或现有技术描述中所需要使用的附图作简单地介绍,显而易见地,下面描述中的附图仅仅是本发明的实施例,对于本领域普通技术人员来讲,在不付出创造性劳动的前提下,还可以根据提供的附图获得其他的附图。In order to explain the embodiments of the present invention or the technical solutions in the prior art more clearly, the following briefly introduces the accompanying drawings that need to be used in the description of the embodiments or the prior art. Obviously, the accompanying drawings in the following description are only It is an embodiment of the present invention. For those of ordinary skill in the art, other drawings can also be obtained according to the provided drawings without creative work.
图1为本发明实施例1中产品的X射线衍射花样;Fig. 1 is the X-ray diffraction pattern of product in the embodiment of the
图2为本发明实施例1中产品的TEM图;Fig. 2 is the TEM image of the product in the embodiment of the
图3为本发明实施例1中产品的元素分布图;Fig. 3 is the element distribution diagram of the product in the embodiment of the
图4为本发明实施例1中产品的X射线光电子能谱分析图;Fig. 4 is the X-ray photoelectron spectroscopy analysis diagram of the product in the embodiment of the
图5为本发明实施例1中产品的HAADF图;Fig. 5 is the HAADF figure of the product in the embodiment of the
图6为本发明实施例1中的电催化剂的线性伏安扫描图;6 is a linear voltammetry scan diagram of the electrocatalyst in Example 1 of the present invention;
图7为本发明实施例2中的电催化剂的线性伏安扫描图;7 is a linear voltammetry scan diagram of the electrocatalyst in Example 2 of the present invention;
图8为本发明实施例3中的电催化剂的线性伏安扫描图;8 is a linear voltammetry scan diagram of the electrocatalyst in Example 3 of the present invention;
图9为本发明实施例4中的电催化剂的线性伏安扫描图;9 is a linear voltammetry scan diagram of the electrocatalyst in Example 4 of the present invention;
图10为本发明实施例5中的电催化剂的线性伏安扫描图;Figure 10 is a linear voltammetry scan diagram of the electrocatalyst in Example 5 of the present invention;
图11为本发明比较例1中的电催化剂的线性伏安扫描图;FIG. 11 is a linear voltammetry scan diagram of the electrocatalyst in Comparative Example 1 of the present invention;
图12为本发明比较例2中的电催化剂的线性伏安扫描图;Figure 12 is a linear voltammetry scan diagram of the electrocatalyst in Comparative Example 2 of the present invention;
图13为本发明实施例1、比较例1和比较例2中的催化剂将二氧化碳还原成一氧化碳的法拉第效率曲线。13 is a Faradaic efficiency curve of the catalysts in Example 1, Comparative Example 1 and Comparative Example 2 of the present invention for reducing carbon dioxide to carbon monoxide.
具体实施方式Detailed ways
本发明提供了一种镍氮共掺杂碳基电催化剂的制备方法,包括以下步骤:The invention provides a preparation method of a nickel-nitrogen co-doped carbon-based electrocatalyst, comprising the following steps:
A)将镍盐、双氰胺和氯化铵在水中分散,干燥后进行煅烧;A) disperse nickel salt, dicyandiamide and ammonium chloride in water, and calcine after drying;
B)将煅烧后的产品与葡萄糖在水中混合后进行水热反应;B) the product after calcination is mixed with glucose in water to carry out hydrothermal reaction;
C)将水热反应的产品进行煅烧,得到镍氮共掺杂碳基电催化剂。C) calcining the product of the hydrothermal reaction to obtain a nickel-nitrogen co-doped carbon-based electrocatalyst.
本发明中的制备方法制得的电催化剂反应选择性高,且成本低。The electrocatalyst prepared by the preparation method of the present invention has high reaction selectivity and low cost.
本发明将镍盐、双氰胺和氯化铵在水中分散,80℃下搅拌后蒸干水分,然后进行煅烧,得到煅烧后的产品。在本发明中,所述镍盐优选为二价可溶性镍盐,更优选为硝酸镍、乙酸镍、氯化镍;所述镍盐与双氰胺的质量比优选为(0.2~5):100,更优选为(1~4):100;所述镍盐与氯化铵的质量比为(0.2~5):500,更优选为(1~4):500。具体的,在本发明的实施例中,可以是1:100:500,3.5:100:500或4.7:100:500。在本发明中,所述首次煅烧的温度优选为500~650℃,更优选为550~600℃;所述首次煅烧的时间优选为1~4小时,更优选为2~3小时。本发明优选以5~10℃/min的速率进行升温,升温至煅烧温度后进行煅烧,煅烧完毕后自然降温。In the present invention, nickel salt, dicyandiamide and ammonium chloride are dispersed in water, the water is evaporated to dryness after stirring at 80 DEG C, and then calcined to obtain a calcined product. In the present invention, the nickel salt is preferably a divalent soluble nickel salt, more preferably nickel nitrate, nickel acetate, and nickel chloride; the mass ratio of the nickel salt to dicyandiamide is preferably (0.2-5):100 , more preferably (1-4):100; the mass ratio of the nickel salt to ammonium chloride is (0.2-5):500, more preferably (1-4):500. Specifically, in the embodiment of the present invention, it may be 1:100:500, 3.5:100:500 or 4.7:100:500. In the present invention, the temperature of the first calcination is preferably 500-650°C, more preferably 550-600°C; the time of the first calcination is preferably 1-4 hours, more preferably 2-3 hours. In the present invention, the temperature is preferably raised at a rate of 5-10°C/min, the temperature is raised to the calcination temperature and then calcined, and the temperature is naturally lowered after the calcination is completed.
所述首次煅烧后的产品和葡萄糖在水中混合后进行水热反应,所述首次煅烧后的产品与葡萄糖的质量比优选为(0.7~1.5):5,更优选为(1~1.2):5.所述水热反应的温度优选为160~200℃,更优选为180~190℃;所述水热反应的时间优选为10~20小时,更优选为12~18小时。水热反应完成后待其自然冷却,然后将水热反应的产物依次用去离子水和乙醇进行清洗,然后干燥。The product after the first calcination and the glucose are mixed in water to carry out a hydrothermal reaction, and the mass ratio of the product after the first calcination to the glucose is preferably (0.7-1.5): 5, more preferably (1-1.2): 5 The temperature of the hydrothermal reaction is preferably 160-200°C, more preferably 180-190°C; the time of the hydrothermal reaction is preferably 10-20 hours, more preferably 12-18 hours. After the hydrothermal reaction is completed, it is allowed to cool naturally, and then the product of the hydrothermal reaction is washed with deionized water and ethanol in sequence, and then dried.
将水热反应的产品进行煅烧,所述煅烧优选在氩气氛围下进行,所述煅烧的温度优选为800~1100℃,更优选为900~1000℃;所述煅烧的时间优选为0.5~4小时,更优选为1~3小时。本发明优选以5~10℃/min的速率升温至所述煅烧温度,然后进行煅烧,煅烧完毕后以5~10℃/min的速率降温至室温,得到镍氮共掺杂碳基电催化剂。The product of the hydrothermal reaction is calcined, and the calcination is preferably carried out under an argon atmosphere. The calcination temperature is preferably 800-1100°C, more preferably 900-1000°C; the calcining time is preferably 0.5-4 hours, more preferably 1 to 3 hours. In the present invention, the temperature is preferably raised to the calcination temperature at a rate of 5-10° C./min, followed by calcination, and after calcination is completed, the temperature is lowered to room temperature at a rate of 5-10° C./min to obtain a nickel-nitrogen co-doped carbon-based electrocatalyst.
本发明还提供了一种镍氮共掺杂碳基电催化剂,按照上述制备方法制得。本发明中的镍氮共掺杂碳基电催化剂中氮的质量分数优选为3~6%,更优选为4%,镍的质量分数优选为1~3%,更优选为1.4%。N元素在催化剂中有石墨氮和吡啶氮两种形式,Ni与吡啶氮相连。催化剂最外层包裹有葡萄糖碳化生成的石墨烯。The present invention also provides a nickel-nitrogen co-doped carbon-based electrocatalyst, which is prepared according to the above preparation method. The mass fraction of nitrogen in the nickel-nitrogen co-doped carbon-based electrocatalyst in the present invention is preferably 3-6%, more preferably 4%, and the mass fraction of nickel is preferably 1-3%, more preferably 1.4%. There are two forms of N element in the catalyst: graphitic nitrogen and pyridine nitrogen, and Ni is connected with pyridine nitrogen. The outermost layer of the catalyst is wrapped with graphene produced by carbonization of glucose.
本发明还提供了上述电催化剂在催化还原二氧化碳反应中的应用。The present invention also provides the application of the above electrocatalyst in the catalytic reduction of carbon dioxide.
本发明提供了一种镍氮共掺杂碳基电催化剂的制备方法,包括以下步骤:A)将镍盐、双氰胺和氯化铵在水中分散,干燥后进行煅烧;B)将煅烧后的产品与葡萄糖在水中混合后进行水热反应;C)将水热反应的产品进行煅烧,得到镍氮共掺杂碳基电催化剂。本发明利用限域反应,将单原子形式的镍分散在氮掺杂的碳基材料中,同时引入葡萄糖最为保护层,避免了高温煅烧过程中活性位点的团聚和流失。所制得的催化剂表现出优异的电催化二氧化碳还原性能,对一氧化碳的选择性可达99%。本发明提供的制备方法具有工艺流程简单、成本低廉、产量大适合于工业生产等特点,具有潜在的应用价值。The present invention provides a method for preparing a nickel-nitrogen co-doped carbon-based electrocatalyst, comprising the following steps: A) dispersing nickel salt, dicyandiamide and ammonium chloride in water, drying and then calcining; B) calcining After mixing the product with glucose in water, a hydrothermal reaction is carried out; C) the product of the hydrothermal reaction is calcined to obtain a nickel-nitrogen co-doped carbon-based electrocatalyst. The invention utilizes the confinement reaction to disperse nickel in the form of single atoms in the nitrogen-doped carbon-based material, and at the same time introduces glucose as the protective layer, so as to avoid the agglomeration and loss of active sites during high-temperature calcination. The prepared catalyst exhibits excellent electrocatalytic carbon dioxide reduction performance, and the selectivity to carbon monoxide can reach 99%. The preparation method provided by the invention has the characteristics of simple process flow, low cost, large output, suitable for industrial production and the like, and has potential application value.
为了进一步说明本发明,以下结合实施例对本发明提供的一种镍氮共掺杂碳基电催化剂、其制备方法及应用进行详细描述,但不能将其理解为对本发明保护范围的限定。In order to further illustrate the present invention, a nickel-nitrogen co-doped carbon-based electrocatalyst provided by the present invention, its preparation method and application will be described in detail below with reference to the examples, but it should not be construed as a limitation on the protection scope of the present invention.
实施例1Example 1
将氯化镍、双氰胺、氯化铵按质量比3.5:100:500和水混合分散,80℃以下搅拌,蒸干;Mix and disperse nickel chloride, dicyandiamide and ammonium chloride with water in a mass ratio of 3.5:100:500, stir below 80°C, and evaporate to dryness;
将蒸干的样品放入坩埚中,以5℃/min的升温速率在500℃煅烧1小时,然后以5℃/min的降温速率降至室温;Put the evaporated samples into a crucible, calcined at 500°C for 1 hour at a heating rate of 5°C/min, and then lowered to room temperature at a cooling rate of 5°C/min;
将煅烧后的样品与葡萄糖以质量比1:5与水混合,然后在180℃下水热反应12小时,得到的产物依次用去离子水和乙醇清洗,然后干燥;The calcined sample and glucose were mixed with water at a mass ratio of 1:5, and then hydrothermally reacted at 180 ° C for 12 hours, and the obtained product was washed with deionized water and ethanol in turn, and then dried;
将水热处理后的样品放置石英管内,以5℃/min的升温速率在1000℃氩气氛围内煅烧0.5小时,然后以5℃/min的降温速率降至室温,得到镍氮共掺杂碳基电催化剂。The hydrothermally treated sample was placed in a quartz tube, calcined at a heating rate of 5°C/min in an argon atmosphere at 1000°C for 0.5 hours, and then lowered to room temperature at a cooling rate of 5°C/min to obtain a nickel-nitrogen co-doped carbon matrix. Electrocatalyst.
采用XRD对制备的样品进行分析,结果见图1。图1为本发明实施例1中产品的X射线衍射花样。由图1可知,图1的谱图与石墨烯的谱图一致,可以判定样品的碳经高温处理变为石墨烯。Ni因为含量少,在石墨烯中并没有结晶,所以谱图中不会出现Ni的衍射峰。The prepared samples were analyzed by XRD, and the results are shown in Figure 1. Fig. 1 is the X-ray diffraction pattern of the product in Example 1 of the present invention. It can be seen from Fig. 1 that the spectrum of Fig. 1 is consistent with the spectrum of graphene, and it can be determined that the carbon of the sample becomes graphene after high temperature treatment. Because of the small content of Ni, it does not crystallize in graphene, so the diffraction peak of Ni does not appear in the spectrum.
对制备的样品进行TEM分析,结果见图2~3。图2为本发明实施例1中产品的TEM图;图3为本发明实施例1中产品的元素分布图。由图2可知,所制备的样品为片状形貌,图3的元素分布图表明镍和氮均匀分布在碳上。The prepared samples were analyzed by TEM, and the results are shown in Figures 2-3. FIG. 2 is a TEM image of the product in Example 1 of the present invention; FIG. 3 is an element distribution diagram of the product in Example 1 of the present invention. It can be seen from Fig. 2 that the prepared sample has a flake-like morphology, and the element distribution map of Fig. 3 shows that nickel and nitrogen are uniformly distributed on the carbon.
对制备的样品进行X射线光电子能谱分析,结果见图4,图4为本发明实施例1中产品的X射线光电子能谱分析图。其中图a是Ni2p的XPS图谱,图b是N1s的XPS图谱,由图4可知N和Ni成功掺入碳中。The prepared sample was subjected to X-ray photoelectron spectroscopy analysis, and the results are shown in Figure 4, which is an X-ray photoelectron spectroscopy analysis diagram of the product in Example 1 of the present invention. Figure a is the XPS spectrum of Ni2p, and Figure b is the XPS spectrum of N1s. It can be seen from Figure 4 that N and Ni were successfully incorporated into carbon.
对制备的样品进行HAADF表征,结果见图5,图5为本发明实施例1中产品的HAADF图。由图5可知,Ni以单原子分散在碳基底上。The prepared samples were characterized by HAADF, and the results are shown in Figure 5, which is the HAADF diagram of the product in Example 1 of the present invention. It can be seen from Fig. 5 that Ni is dispersed on the carbon substrate as a single atom.
实施例2Example 2
将氯化镍、双氰胺、氯化铵按质量比1:100:500和水混合分散,80℃以下搅拌,蒸干;Mix and disperse nickel chloride, dicyandiamide and ammonium chloride with water in a mass ratio of 1:100:500, stir below 80°C, and evaporate to dryness;
将蒸干的样品放入坩埚中,以5℃/min的升温速率在550℃煅烧2小时,然后以5℃/min的降温速率降至室温;Put the evaporated samples into a crucible, calcine at 550°C for 2 hours at a heating rate of 5°C/min, and then drop to room temperature at a cooling rate of 5°C/min;
将煅烧后的样品与葡萄糖以质量比1:5与水混合,然后在180℃下水热反应12小时,得到的产物依次用去离子水和乙醇清洗,然后干燥;The calcined sample and glucose were mixed with water at a mass ratio of 1:5, and then hydrothermally reacted at 180 ° C for 12 hours, and the obtained product was washed with deionized water and ethanol in turn, and then dried;
将水热处理后的样品放置石英管内,以5℃/min的升温速率在1000℃氩气氛围内煅烧1小时,然后以5℃/min的降温速率降至室温,得到镍氮共掺杂碳基电催化剂。The hydrothermally treated sample was placed in a quartz tube, calcined at a heating rate of 5°C/min in an argon atmosphere of 1000°C for 1 hour, and then lowered to room temperature at a cooling rate of 5°C/min to obtain a nickel-nitrogen co-doped carbon matrix. Electrocatalyst.
实施例3Example 3
将氯化镍、双氰胺、氯化铵按质量比4.7:100:500和水混合分散,80℃以下搅拌,蒸干;Mix and disperse nickel chloride, dicyandiamide and ammonium chloride with water in a mass ratio of 4.7:100:500, stir below 80°C, and evaporate to dryness;
将蒸干的样品放入坩埚中,以5℃/min的升温速率在600℃煅烧3小时,然后以5℃/min的降温速率降至室温;Put the evaporated samples into a crucible, calcined at 600°C for 3 hours at a heating rate of 5°C/min, and then lowered to room temperature at a cooling rate of 5°C/min;
将煅烧后的样品与葡萄糖以质量比1:5与水混合,然后在160℃下水热反应16小时,得到的产物依次用去离子水和乙醇清洗,然后干燥;The calcined sample and glucose were mixed with water at a mass ratio of 1:5, and then hydrothermally reacted at 160 ° C for 16 hours, and the obtained product was washed with deionized water and ethanol in turn, and then dried;
将水热处理后的样品放置石英管内,以5℃/min的升温速率在1000℃氩气氛围内煅烧3小时,然后以5℃/min的降温速率降至室温,得到镍氮共掺杂碳基电催化剂。The hydrothermally treated sample was placed in a quartz tube, calcined at a heating rate of 5°C/min in an argon atmosphere of 1000°C for 3 hours, and then lowered to room temperature at a cooling rate of 5°C/min to obtain a nickel-nitrogen co-doped carbon matrix. Electrocatalyst.
实施例4Example 4
将氯化镍、双氰胺、氯化铵按质量比3.5:100:500和水混合分散,80℃以下搅拌,蒸干;Mix and disperse nickel chloride, dicyandiamide and ammonium chloride with water in a mass ratio of 3.5:100:500, stir below 80°C, and evaporate to dryness;
将蒸干的样品放入坩埚中,以5℃/min的升温速率在500℃煅烧1小时,然后以5℃/min的降温速率降至室温;Put the evaporated samples into a crucible, calcined at 500°C for 1 hour at a heating rate of 5°C/min, and then lowered to room temperature at a cooling rate of 5°C/min;
将煅烧后的样品与葡萄糖以质量比1:5与水混合,然后在180℃下水热反应12小时,得到的产物依次用去离子水和乙醇清洗,然后干燥;The calcined sample and glucose were mixed with water at a mass ratio of 1:5, and then hydrothermally reacted at 180 ° C for 12 hours, and the obtained product was washed with deionized water and ethanol in turn, and then dried;
将水热处理后的样品放置石英管内,以5℃/min的升温速率在1100℃氩气氛围内煅烧0.5小时,然后以5℃/min的降温速率降至室温,得到镍氮共掺杂碳基电催化剂。The hydrothermally treated sample was placed in a quartz tube, calcined at a heating rate of 5°C/min in an argon atmosphere at 1100°C for 0.5 hours, and then lowered to room temperature at a cooling rate of 5°C/min to obtain a nickel-nitrogen co-doped carbon matrix. Electrocatalyst.
实施例5Example 5
将氯化镍、双氰胺、氯化铵按质量比3.5:100:500和水混合分散,80℃以下搅拌,蒸干;Mix and disperse nickel chloride, dicyandiamide and ammonium chloride with water in a mass ratio of 3.5:100:500, stir below 80°C, and evaporate to dryness;
将蒸干的样品放入坩埚中,以5℃/min的升温速率在500℃煅烧1小时,然后以5℃/min的降温速率降至室温;Put the evaporated samples into a crucible, calcined at 500°C for 1 hour at a heating rate of 5°C/min, and then lowered to room temperature at a cooling rate of 5°C/min;
将煅烧后的样品与葡萄糖以质量比1:5与水混合,然后在180℃下水热反应12小时,得到的产物依次用去离子水和乙醇清洗,然后干燥;The calcined sample and glucose were mixed with water at a mass ratio of 1:5, and then hydrothermally reacted at 180 ° C for 12 hours, and the obtained product was washed with deionized water and ethanol in turn, and then dried;
将水热处理后的样品放置石英管内,以5℃/min的升温速率在800℃氩气氛围内煅烧0.5小时,然后以5℃/min的降温速率降至室温,得到镍氮共掺杂碳基电催化剂。The hydrothermally treated sample was placed in a quartz tube, calcined at a heating rate of 5°C/min in an argon atmosphere of 800°C for 0.5 hours, and then lowered to room temperature at a cooling rate of 5°C/min to obtain a nickel-nitrogen co-doped carbon matrix. Electrocatalyst.
比较例1Comparative Example 1
将双氰胺、氯化铵按质量比2:10和水混合分散,80℃以下搅拌,蒸干;Mix and disperse dicyandiamide and ammonium chloride with water in a mass ratio of 2:10, stir below 80°C, and evaporate to dryness;
将蒸干的样品放入坩埚中,以5℃/min的升温速率在500℃煅烧1小时,然后以5℃/min的降温速率降至室温;Put the evaporated samples into a crucible, calcined at 500°C for 1 hour at a heating rate of 5°C/min, and then lowered to room temperature at a cooling rate of 5°C/min;
将煅烧后的样品与葡萄糖以质量比1:5与水混合,然后在180℃下水热反应12小时,得到的产物依次用去离子水和乙醇清洗,然后干燥;The calcined sample and glucose were mixed with water at a mass ratio of 1:5, and then hydrothermally reacted at 180 ° C for 12 hours, and the obtained product was washed with deionized water and ethanol in turn, and then dried;
将水热处理后的样品放置石英管内,以5℃/min的升温速率在1000℃氩气氛围内煅烧0.5小时,然后以5℃/min的降温速率降至室温,得到氮掺杂碳基电催化剂。The hydrothermally treated sample was placed in a quartz tube, calcined at a heating rate of 5°C/min in an argon atmosphere at 1000°C for 0.5 hours, and then lowered to room temperature at a cooling rate of 5°C/min to obtain a nitrogen-doped carbon-based electrocatalyst. .
比较例2Comparative Example 2
将氯化镍、双氰胺、氯化铵按质量比3.5:100:500和水混合分散,80℃以下搅拌,蒸干;Mix and disperse nickel chloride, dicyandiamide and ammonium chloride with water in a mass ratio of 3.5:100:500, stir below 80°C, and evaporate to dryness;
将蒸干的样品放入坩埚中,以5℃/min的升温速率在500℃煅烧1小时,然后以5℃/min的降温速率降至室温;Put the evaporated samples into a crucible, calcined at 500°C for 1 hour at a heating rate of 5°C/min, and then lowered to room temperature at a cooling rate of 5°C/min;
将煅烧后的样品放置石英管内,以5℃/min的升温速率在1000℃氩气氛围内煅烧0.5小时,然后以5℃/min的降温速率降至室温,得到碳基电催化剂。The calcined samples were placed in a quartz tube, calcined at a heating rate of 5 °C/min in an argon atmosphere at 1000 °C for 0.5 h, and then lowered to room temperature at a cooling rate of 5 °C/min to obtain a carbon-based electrocatalyst.
本发明检测了实施例1~5和比较例1~2得到的电催化剂对二氧化碳的还原活性,结果如图6~12所示,图6为本发明实施例1中的电催化剂的线性伏安扫描图;图7为本发明实施例2中的电催化剂的线性伏安扫描图;图8为本发明实施例3中的电催化剂的线性伏安扫描图;图9为本发明实施例4中的电催化剂的线性伏安扫描图;图10为本发明实施例5中的电催化剂的线性伏安扫描图;图11为本发明比较例1中的电催化剂的线性伏安扫描图;图12为本发明比较例2中的电催化剂的线性伏安扫描图;由上述线性伏安扫描图可以看出,本发明实施例1~5中的催化剂具有良好的二氧化碳还原活性,而比较例1和比较例2中的催化剂还原活性较差。In the present invention, the reduction activities of the electrocatalysts obtained in Examples 1 to 5 and Comparative Examples 1 to 2 were tested for carbon dioxide reduction. Scanning diagram; FIG. 7 is the linear voltammetric scan diagram of the electrocatalyst in Example 2 of the present invention; FIG. 8 is the linear voltammetric scan diagram of the electrocatalyst in Example 3 of the present invention; FIG. 9 is the example 4 of the present invention. The linear voltammetry scan diagram of the electrocatalyst; Figure 10 is the linear voltammetry scan diagram of the electrocatalyst in Example 5 of the present invention; Figure 11 is the linear voltammetry scan diagram of the electrocatalyst in Comparative Example 1 of the present invention; Figure 12 It is the linear voltammogram of the electrocatalyst in Comparative Example 2 of the present invention; it can be seen from the above linear voltammogram that the catalysts in Examples 1 to 5 of the present invention have good carbon dioxide reduction activity, while Comparative Examples 1 and 5 have good carbon dioxide reduction activity. The catalyst in Comparative Example 2 had poor reducing activity.
本发明测试了实施例1、比较例1和比较例2得到的电催化剂的法拉第效率,结果如图13所示,图13为本发明实施例1、比较例1和比较例2中的催化剂将二氧化碳还原成一氧化碳的法拉第效率曲线。由图13可以看出,本发明实施例1中的镍氮共掺杂碳基电催化剂具有较高的法拉第效率,对二氧化碳还原反应的选择性高达99%,而比较例1和比较例2中的催化剂的法拉第效率最高不到70%。The present invention tested the Faradaic efficiency of the electrocatalysts obtained in Example 1, Comparative Example 1 and Comparative Example 2. The results are shown in Figure 13. Figure 13 shows that the catalysts in Example 1, Comparative Example 1 and Comparative Example 2 of the present invention will Faradaic efficiency curve for the reduction of carbon dioxide to carbon monoxide. It can be seen from FIG. 13 that the nickel-nitrogen co-doped carbon-based electrocatalyst in Example 1 of the present invention has a higher Faradaic efficiency, and the selectivity for carbon dioxide reduction reaction is as high as 99%, while that in Comparative Example 1 and Comparative Example 2 is as high as 99%. The faradaic efficiency of the catalyst is less than 70% at best.
以上所述仅是本发明的优选实施方式,应当指出,对于本技术领域的普通技术人员来说,在不脱离本发明原理的前提下,还可以做出若干改进和润饰,这些改进和润饰也应视为本发明的保护范围。The above are only the preferred embodiments of the present invention. It should be pointed out that for those skilled in the art, without departing from the principles of the present invention, several improvements and modifications can be made. It should be regarded as the protection scope of the present invention.
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