CN114570344A - Transition metal monatomic catalyst and preparation method and application thereof - Google Patents
Transition metal monatomic catalyst and preparation method and application thereof Download PDFInfo
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- 239000003054 catalyst Substances 0.000 title claims abstract description 118
- 229910052723 transition metal Inorganic materials 0.000 title claims abstract description 74
- 150000003624 transition metals Chemical class 0.000 title claims abstract description 59
- 238000002360 preparation method Methods 0.000 title claims abstract description 21
- MCMNRKCIXSYSNV-UHFFFAOYSA-N Zirconium dioxide Chemical compound O=[Zr]=O MCMNRKCIXSYSNV-UHFFFAOYSA-N 0.000 claims abstract description 54
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 claims abstract description 48
- 230000001699 photocatalysis Effects 0.000 claims abstract description 28
- 230000009467 reduction Effects 0.000 claims abstract description 28
- 229910002092 carbon dioxide Inorganic materials 0.000 claims abstract description 25
- 239000001569 carbon dioxide Substances 0.000 claims abstract description 23
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 claims abstract description 16
- 229910002091 carbon monoxide Inorganic materials 0.000 claims abstract description 16
- QCWXUUIWCKQGHC-UHFFFAOYSA-N Zirconium Chemical class [Zr] QCWXUUIWCKQGHC-UHFFFAOYSA-N 0.000 claims description 19
- -1 transition metal salt Chemical class 0.000 claims description 17
- 238000000034 method Methods 0.000 claims description 16
- 238000006243 chemical reaction Methods 0.000 claims description 12
- 239000000243 solution Substances 0.000 claims description 12
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Chemical compound O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 12
- 239000012670 alkaline solution Substances 0.000 claims description 9
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- RKTYLMNFRDHKIL-UHFFFAOYSA-N copper;5,10,15,20-tetraphenylporphyrin-22,24-diide Chemical compound [Cu+2].C1=CC(C(=C2C=CC([N-]2)=C(C=2C=CC=CC=2)C=2C=CC(N=2)=C(C=2C=CC=CC=2)C2=CC=C3[N-]2)C=2C=CC=CC=2)=NC1=C3C1=CC=CC=C1 RKTYLMNFRDHKIL-UHFFFAOYSA-N 0.000 claims description 3
- 238000001035 drying Methods 0.000 claims description 3
- QTBSBXVTEAMEQO-UHFFFAOYSA-M Acetate Chemical compound CC([O-])=O QTBSBXVTEAMEQO-UHFFFAOYSA-M 0.000 claims description 2
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- CDBYLPFSWZWCQE-UHFFFAOYSA-L Sodium Carbonate Chemical compound [Na+].[Na+].[O-]C([O-])=O CDBYLPFSWZWCQE-UHFFFAOYSA-L 0.000 claims 2
- UIIMBOGNXHQVGW-UHFFFAOYSA-M Sodium bicarbonate Chemical compound [Na+].OC([O-])=O UIIMBOGNXHQVGW-UHFFFAOYSA-M 0.000 claims 2
- 150000003841 chloride salts Chemical class 0.000 claims 1
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- 230000000694 effects Effects 0.000 abstract description 8
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- RVTZCBVAJQQJTK-UHFFFAOYSA-N oxygen(2-);zirconium(4+) Chemical compound [O-2].[O-2].[Zr+4] RVTZCBVAJQQJTK-UHFFFAOYSA-N 0.000 abstract 2
- 229910001928 zirconium oxide Inorganic materials 0.000 abstract 2
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- OERNJTNJEZOPIA-UHFFFAOYSA-N zirconium nitrate Chemical compound [Zr+4].[O-][N+]([O-])=O.[O-][N+]([O-])=O.[O-][N+]([O-])=O.[O-][N+]([O-])=O OERNJTNJEZOPIA-UHFFFAOYSA-N 0.000 description 8
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- CPLXHLVBOLITMK-UHFFFAOYSA-N Magnesium oxide Chemical compound [Mg]=O CPLXHLVBOLITMK-UHFFFAOYSA-N 0.000 description 4
- 238000002354 inductively-coupled plasma atomic emission spectroscopy Methods 0.000 description 4
- 238000003786 synthesis reaction Methods 0.000 description 4
- 238000006555 catalytic reaction Methods 0.000 description 3
- 229910052802 copper Inorganic materials 0.000 description 3
- 230000002950 deficient Effects 0.000 description 3
- 239000008367 deionised water Substances 0.000 description 3
- 229910021641 deionized water Inorganic materials 0.000 description 3
- 238000010586 diagram Methods 0.000 description 3
- 239000002638 heterogeneous catalyst Substances 0.000 description 3
- 239000012621 metal-organic framework Chemical group 0.000 description 3
- KBJMLQFLOWQJNF-UHFFFAOYSA-N nickel(ii) nitrate Chemical compound [Ni+2].[O-][N+]([O-])=O.[O-][N+]([O-])=O KBJMLQFLOWQJNF-UHFFFAOYSA-N 0.000 description 3
- 238000013032 photocatalytic reaction Methods 0.000 description 3
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- 229910018072 Al 2 O 3 Inorganic materials 0.000 description 2
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 description 2
- 229910021586 Nickel(II) chloride Inorganic materials 0.000 description 2
- 229910004298 SiO 2 Inorganic materials 0.000 description 2
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 2
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- CKUAXEQHGKSLHN-UHFFFAOYSA-N [C].[N] Chemical compound [C].[N] CKUAXEQHGKSLHN-UHFFFAOYSA-N 0.000 description 2
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- 230000009286 beneficial effect Effects 0.000 description 2
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- HSJPMRKMPBAUAU-UHFFFAOYSA-N cerium(3+);trinitrate Chemical compound [Ce+3].[O-][N+]([O-])=O.[O-][N+]([O-])=O.[O-][N+]([O-])=O HSJPMRKMPBAUAU-UHFFFAOYSA-N 0.000 description 2
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- QMMRZOWCJAIUJA-UHFFFAOYSA-L nickel dichloride Chemical compound Cl[Ni]Cl QMMRZOWCJAIUJA-UHFFFAOYSA-L 0.000 description 2
- LGQLOGILCSXPEA-UHFFFAOYSA-L nickel sulfate Chemical compound [Ni+2].[O-]S([O-])(=O)=O LGQLOGILCSXPEA-UHFFFAOYSA-L 0.000 description 2
- 229910000363 nickel(II) sulfate Inorganic materials 0.000 description 2
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- 150000003839 salts Chemical class 0.000 description 2
- 229910052726 zirconium Inorganic materials 0.000 description 2
- DUFCMRCMPHIFTR-UHFFFAOYSA-N 5-(dimethylsulfamoyl)-2-methylfuran-3-carboxylic acid Chemical compound CN(C)S(=O)(=O)C1=CC(C(O)=O)=C(C)O1 DUFCMRCMPHIFTR-UHFFFAOYSA-N 0.000 description 1
- GRYLNZFGIOXLOG-UHFFFAOYSA-N Nitric acid Chemical compound O[N+]([O-])=O GRYLNZFGIOXLOG-UHFFFAOYSA-N 0.000 description 1
- GEIAQOFPUVMAGM-UHFFFAOYSA-N Oxozirconium Chemical group [Zr]=O GEIAQOFPUVMAGM-UHFFFAOYSA-N 0.000 description 1
- 238000003917 TEM image Methods 0.000 description 1
- GWEVSGVZZGPLCZ-UHFFFAOYSA-N Titan oxide Chemical compound O=[Ti]=O GWEVSGVZZGPLCZ-UHFFFAOYSA-N 0.000 description 1
- DGEZNRSVGBDHLK-UHFFFAOYSA-N [1,10]phenanthroline Chemical compound C1=CN=C2C3=NC=CC=C3C=CC2=C1 DGEZNRSVGBDHLK-UHFFFAOYSA-N 0.000 description 1
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- 238000007254 oxidation reaction Methods 0.000 description 1
- BMMGVYCKOGBVEV-UHFFFAOYSA-N oxo(oxoceriooxy)cerium Chemical compound [Ce]=O.O=[Ce]=O BMMGVYCKOGBVEV-UHFFFAOYSA-N 0.000 description 1
- 238000007539 photo-oxidation reaction Methods 0.000 description 1
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- OGIDPMRJRNCKJF-UHFFFAOYSA-N titanium oxide Inorganic materials [Ti]=O OGIDPMRJRNCKJF-UHFFFAOYSA-N 0.000 description 1
- XJDNKRIXUMDJCW-UHFFFAOYSA-J titanium tetrachloride Chemical compound Cl[Ti](Cl)(Cl)Cl XJDNKRIXUMDJCW-UHFFFAOYSA-J 0.000 description 1
- 229910001428 transition metal ion Inorganic materials 0.000 description 1
- 238000005303 weighing Methods 0.000 description 1
- 150000003754 zirconium Chemical class 0.000 description 1
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- B01J21/00—Catalysts comprising the elements, oxides, or hydroxides of magnesium, boron, aluminium, carbon, silicon, titanium, zirconium, or hafnium
- B01J21/06—Silicon, titanium, zirconium or hafnium; Oxides or hydroxides thereof
- B01J21/066—Zirconium or hafnium; Oxides or hydroxides thereof
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Abstract
Description
技术领域technical field
本发明涉及微纳米材料制备技术领域。更具体地,涉及一种过渡金属单原子催化剂及其制备方法和应用。The invention relates to the technical field of preparation of micro-nano materials. More specifically, it relates to a transition metal single-atom catalyst and its preparation method and application.
背景技术Background technique
单原子型多相催化剂作为一种沟通均相催化剂和非均相催化剂桥梁,即保留了均相催化剂对催化反应高活性、高选择性的特点,又具有非均相催化剂在催化反应中易于分离的优势,成为了催化剂设计的热门领域,代表了该领域的发展方向。As a bridge between homogeneous catalysts and heterogeneous catalysts, single-atom heterogeneous catalysts not only retain the characteristics of high activity and high selectivity of homogeneous catalysts for catalytic reactions, but also have the characteristics of easy separation of heterogeneous catalysts in catalytic reactions. It has become a hot field of catalyst design and represents the development direction of this field.
然而,近些年来,受到单个原子高的表面能、在制备和应用中极易团聚的影响,鲜有直接研究一步法制备氧化物锚定的过渡金属单原子光催化剂的报道。现有技术中比较成熟的例子有碳-氮载体锚定过渡金属单原子或者金属有机框架结构载体锚定过渡金属单原子。例如张铁锐老师课题组通过邻菲罗啉与过渡金属配位,实现了大规模合成碳-氮载体锚定的过渡金属单原子催化剂[Nat.Commun.2019,10:4585];李亚栋老师课题组通过MOF封装方法,实现了大规模合成金属有机框架结构载体锚定的过渡金属单原子催化剂[Nat.Catal.2018,1,935-945]。但是,上述两种载体合成过渡金属单原子催化剂的单原子的配位方式是金属-碳/氮结构(M-C/N),该类结构在光催化反应中易于被光生空穴和活性氧所破坏,因此在实际光催化应用中需要大量的牺牲剂来维持稳定。解决这一问题的办法是开发出来金属-氧配(M-O)位结构的单原子催化剂,可以从本质上提升单原子催化剂的稳定性。However, in recent years, due to the high surface energy of a single atom and its easy agglomeration in preparation and application, few reports have directly investigated the one-step preparation of oxide-anchored transition metal single-atom photocatalysts. The relatively mature examples in the prior art include carbon-nitrogen support for anchoring transition metal single atoms or metal organic framework structure support for anchoring transition metal single atoms. For example, Zhang Tierui's research group has achieved large-scale synthesis of carbon-nitrogen carrier-anchored transition metal single-atom catalysts through the coordination of phenanthroline and transition metals [Nat.Commun.2019, 10:4585]; Li Yadong's research group has passed The MOF encapsulation method has enabled the large-scale synthesis of metal-organic framework structure support-anchored transition metal single-atom catalysts [Nat. Catal. 2018, 1, 935-945]. However, the coordination mode of the single atoms of the above two supports for the synthesis of transition metal single-atom catalysts is a metal-carbon/nitrogen structure (M-C/N), which is easily destroyed by photo-generated holes and reactive oxygen species in the photocatalytic reaction. , so a large amount of sacrificial agent is required to maintain stability in practical photocatalytic applications. The solution to this problem is to develop single-atom catalysts with a metal-oxygen coordination (M-O) structure, which can substantially improve the stability of single-atom catalysts.
然而,现有技术中用于合成金属-氧配位结构的过渡金属单原子催化剂的金属氧化物载体主要为CeO2,FeOx,Al2O3,TiO2,MgO,SiO2,WOx和ZnO。然而,这些载体并不能很好的传导光电子。However, the metal oxide supports used in the prior art to synthesize transition metal single-atom catalysts with metal-oxygen coordination structures are mainly CeO 2 , FeO x , Al 2 O 3 , TiO 2 , MgO, SiO 2 , WO x and ZnO. However, these carriers do not conduct photoelectrons well.
发明内容SUMMARY OF THE INVENTION
基于以上问题,本发明的第一个目的在于提供一种过渡金属单原子催化剂,该催化剂以ZrO2为载体,具有高的过渡金属单原子负载量。此外,该催化剂为一种新型的氧化锆载体锚定过渡金属单原子的光催化剂,将其用于光催化二氧化碳还原制备一氧化碳的应用中,具有较高的一氧化碳产物选择性和生成活性。Based on the above problems, the first object of the present invention is to provide a transition metal single-atom catalyst, which uses ZrO 2 as a carrier and has a high transition metal single-atom loading. In addition, the catalyst is a new type of photocatalyst with zirconia carrier anchoring transition metal single atoms, which is used in the application of photocatalytic reduction of carbon dioxide to prepare carbon monoxide, and has high carbon monoxide product selectivity and generation activity.
本发明的第二个目的在于提供一种过渡金属单原子催化剂的制备方法。该制备方法具有适用于多种过渡金属单原子催化剂制备,且制备温度低,活性组分过渡金属单原子负载量大的优点。The second object of the present invention is to provide a preparation method of a transition metal single-atom catalyst. The preparation method has the advantages that it is suitable for the preparation of various transition metal single-atom catalysts, and has the advantages of low preparation temperature and large loading of the active component transition metal single-atom catalyst.
本发明的第三个目的在于提供一种过渡金属单原子催化剂的应用。该催化剂具有较高的选择性和活性。The third object of the present invention is to provide the application of a transition metal single-atom catalyst. The catalyst has high selectivity and activity.
为达到上述第一个目的,本发明采用下述技术方案:For reaching above-mentioned first purpose, the present invention adopts following technical scheme:
一种过渡金属单原子催化剂,所述催化剂以过渡金属单原子为活性组分,以氧化锆(ZrO2)为载体,过渡金属单原子分散于氧化锆的表面和内部。A transition metal single-atom catalyst, the catalyst uses a transition metal single atom as an active component and zirconia (ZrO 2 ) as a carrier, and the transition metal single atom is dispersed on the surface and inside of the zirconia.
本发明的催化剂中,过渡金属以单原子形态分散于载体氧化锆的表面和内部,也即氧化锆锚定的过渡金属单原子催化剂。该催化剂中,过渡金属单原子分散在氧化锆载体的缺陷位中。氧化锆作为一种非还原型载体,在光、热催化作用中都具有着较高的稳定性。其次,氧化锆中锆元素的氧化态为四价,d轨道构型为d0构型,利于紫外光吸收的转化。In the catalyst of the present invention, the transition metal is dispersed on the surface and inside of the carrier zirconia in the form of single atoms, that is, the transition metal single-atom catalyst anchored by the zirconia. In this catalyst, single atoms of transition metals are dispersed in the defect sites of the zirconia support. As a non-reducing carrier, zirconia has high stability in light and thermal catalysis. Secondly, the oxidation state of zirconium element in zirconia is tetravalent, and the d orbital configuration is d0 configuration, which is beneficial to the conversion of ultraviolet light absorption.
相比于前述CeO2,FeOx,Al2O3,TiO2,MgO,SiO2,WOx和ZnO载体,ZrO2载体具有萤石类结构,充满了丰富的弗伦克尔缺陷,即晶体结构表现出偶极矩,利于传导光生电子。其次,ZrO2载体定性强。所以其本身利于锚定单原子,并保持良好的电荷传导能力和结构稳定性。Compared to the aforementioned CeO 2 , FeO x , Al 2 O 3 , TiO 2 , MgO, SiO 2 , WO x and ZnO supports, ZrO 2 supports have a fluorite-like structure filled with abundant Frenkel defects, i.e. crystals The structure exhibits a dipole moment that facilitates conduction of photogenerated electrons. Secondly, the ZrO 2 carrier is qualitatively strong. Therefore, it is conducive to anchoring single atoms and maintains good charge conductivity and structural stability.
进一步地,以该催化剂的总重量为100%计,过渡金属单原子的负载量为1.8~3wt%。Further, based on the total weight of the catalyst as 100%, the loading amount of transition metal single atoms is 1.8-3 wt%.
进一步地,所述过渡金属单原子选自Zn、Ni、Fe、Co或Cu中的一种或几种。Further, the transition metal single atom is selected from one or more of Zn, Ni, Fe, Co or Cu.
进一步地,所述氧化锆为四方晶相,单斜晶相或其混合晶相。优选为四方晶相,其吸光范围广,锆氧结构稳定,更利于光催化反应中。Further, the zirconia is a tetragonal crystal phase, a monoclinic crystal phase or a mixed crystal phase thereof. It is preferably a tetragonal crystal phase, which has a wide light absorption range and a stable zirconium-oxygen structure, which is more conducive to photocatalytic reactions.
为达到上述第二个目的,本发明采用下述技术方案:In order to achieve above-mentioned second purpose, the present invention adopts following technical scheme:
一种过渡金属单原子催化剂的制备方法,包括如下步骤:A preparation method of transition metal single-atom catalyst, comprising the steps:
将过渡金属盐和锆金属盐溶于溶剂中,混合均匀,得澄清透明溶液;Dissolve the transition metal salt and the zirconium metal salt in the solvent and mix them evenly to obtain a clear and transparent solution;
加入碱性溶液,得到反应液;Add alkaline solution to obtain reaction solution;
将反应液进行搅拌反应,干燥,得粗产物;The reaction solution was stirred and reacted, and dried to obtain a crude product;
将粗产物置于空气气氛中,煅烧,降温至室温,洗涤,烘干,得所述过渡金属单原子催化剂。The crude product is placed in an air atmosphere, calcined, cooled to room temperature, washed and dried to obtain the transition metal single-atom catalyst.
本发明的制备方法中,将过渡金属盐、锆金属盐和碱性溶液混合后后,可通过搅拌、超声等方式,促进过渡金属盐、锆金属盐在碱性溶液中溶解和分散,得到胶体状的产物,代表了络合反应的完成。In the preparation method of the present invention, after the transition metal salt, the zirconium metal salt and the alkaline solution are mixed, the transition metal salt and the zirconium metal salt can be dissolved and dispersed in the alkaline solution by means of stirring, ultrasonic, etc., to obtain a colloid The resulting product represents the completion of the complexation reaction.
与传统的制备缺陷位锚定单原子的金属氧化物单原子催化剂的方法相比,本发明是以一步混合、煅烧、洗涤的路径完成的,而传统的方法往往需要预先制备好氧化物载体,然后刻蚀出缺陷,再通过浸渍法才能得到过渡金属单原子催化剂。因此,相比传统方法,本发明的合成过程简单。Compared with the traditional method for preparing a metal oxide single-atom catalyst with defect site anchoring single atoms, the present invention is completed by a one-step mixing, calcining and washing route, while the traditional method often requires pre-preparing an oxide carrier, and then Defects are etched, and then the transition metal single-atom catalyst can be obtained by impregnation method. Therefore, compared with the traditional method, the synthesis process of the present invention is simple.
进一步地,所述煅烧的条件为:以2~10℃·min-1升温速率升温到300~600℃,煅烧1~5h。在该条件下加热升温过程中,使胶体状产物慢慢脱水、不稳定的组分慢慢挥发,达到在氧化锆前驱体上制造缺陷的目的。同时,这个缓慢的低温加热过程也可以使得过渡金属离子很好的分散在此时的胶体产物中。随后,将此胶体状产物进行煅烧,彻底的除去组分中的水等易挥发物质,提升结晶度。Further, the calcination conditions are as follows: the temperature is raised to 300-600° C. at a heating rate of 2-10° C.·min −1 , and calcined for 1-5 hours. During the heating and heating process under this condition, the colloidal product is slowly dehydrated, and the unstable components are slowly volatilized, so as to achieve the purpose of creating defects on the zirconia precursor. At the same time, this slow low-temperature heating process can also make the transition metal ions well dispersed in the colloidal product at this time. Subsequently, the colloidal product is calcined to completely remove volatile substances such as water in the components and improve the crystallinity.
进一步地,所述反应液中,过渡金属盐、锆金属盐的质量比值为1:20~1:50。Further, in the reaction solution, the mass ratio of the transition metal salt and the zirconium metal salt is 1:20-1:50.
进一步地,所述过渡金属盐和锆金属盐在碱性溶液中的质量浓度为13~16mg·mL-1。Further, the mass concentration of the transition metal salt and the zirconium metal salt in the alkaline solution is 13-16 mg·mL -1 .
进一步地,本发明所述的过渡金属盐可以是可分散于碱性溶液中的任何过渡金属盐。所述过渡金属盐包括但不限于选自过渡金属氯盐、过渡金属硝酸盐、过渡金属乙酸盐、过渡金属硫酸盐中的一种或多种。Further, the transition metal salt described in the present invention can be any transition metal salt that can be dispersed in an alkaline solution. The transition metal salts include, but are not limited to, one or more selected from transition metal chlorides, transition metal nitrates, transition metal acetates, and transition metal sulfates.
进一步地,所述锆金属盐选自锆金属氯盐、锆金属硝酸盐、锆金属乙酸盐、锆金属硫酸盐中的一种或多种。Further, the zirconium metal salt is selected from one or more of zirconium metal chloride, zirconium metal nitrate, zirconium metal acetate, and zirconium metal sulfate.
进一步地,所述碱性溶液为NaOH、NaHCO3、Na2CO3、(NH4)2CO3中的一种或多种物质的水溶液,优选为NaHCO3,(NH4)2CO3的水溶液。作为一种弱碱性,热分解可去除的碱性物质,更易于调控形成胶状前驱体中的金属离子配位状况。Further, the alkaline solution is an aqueous solution of one or more substances in NaOH, NaHCO 3 , Na 2 CO 3 , (NH 4 ) 2 CO 3 , preferably NaHCO 3 , (NH 4 ) 2 CO 3 aqueous solution. As a weakly alkaline substance that can be removed by thermal decomposition, it is easier to control the coordination state of metal ions in the formation of colloidal precursors.
进一步地,所述搅拌反应的温度为40~80℃,时间为2~8h。Further, the temperature of the stirring reaction is 40-80° C., and the time is 2-8 h.
进一步地,所述洗涤为用稀酸、水溶液洗涤3~5次。Further, the washing is 3 to 5 times of washing with dilute acid and aqueous solution.
进一步地,所述稀酸选自稀盐酸、稀硫酸、稀硝酸中的一种或多种。Further, the dilute acid is selected from one or more of dilute hydrochloric acid, dilute sulfuric acid, and dilute nitric acid.
进一步地,所述烘干的温度为60~90℃,时间为1~5h。Further, the drying temperature is 60-90° C., and the time is 1-5 h.
为达到上述第三个目的,本发明采用下述技术方案:In order to achieve the above-mentioned third purpose, the present invention adopts following technical scheme:
如上第一个目的所述的过渡金属单原子催化剂在光催化二氧化碳还原制备一氧化碳中的应用。The application of the transition metal single-atom catalyst described in the first object above in the photocatalytic reduction of carbon dioxide to prepare carbon monoxide.
具体地,该反应的化学式为CO2+H2O=CO+H2+O2。Specifically, the chemical formula of this reaction is CO 2 +H 2 O=CO+H 2 +O 2 .
进一步地,所述应用包括如下步骤:Further, the application includes the following steps:
在0.01-1Mpa压力及所述催化剂存在的条件下,全光谱光照CO2和水蒸气的混合气。Under the conditions of 0.01-1Mpa pressure and the presence of the catalyst, the mixture of CO2 and water vapor is illuminated in full spectrum.
进一步地,催化剂的用量为0.01-1g/0.01-0.1L混合气。Further, the dosage of the catalyst is 0.01-1 g/0.01-0.1 L mixed gas.
本发明的有益效果如下:The beneficial effects of the present invention are as follows:
本发明提供的过渡金属单原子催化剂,以过渡金属单原子为活性组分,以氧化锆为载体,是一种新型的氧化锆载体锚定过渡金属单原子的光催化剂。该光催化剂的载体为具有缺陷位的氧化锆,缺陷位的存在为实现稳定的过渡金属单原子锚定提供了可能。同时,缺陷位锚定后的过渡金属单原子由于强金属载体相互作用使其在催化应用中不易发生团聚,可以极大的提升其在光催化反应中的稳定性。在该过渡金属单原子光催化剂的应用中,凭借着过渡金属单原子特殊的不饱和配位状态,可以实现高活性,高选择性的气固相二氧化碳还原为一氧化碳的性能。此外,由于缺陷位锚定过渡金属单原子的稳定性,避免了依靠牺牲剂的使用来克服该催化剂的光氧化/光腐蚀。因此,该制备方法成本低廉、工艺简单,并且在实际应用中充满前景。The transition metal single-atom catalyst provided by the invention uses the transition metal single atom as the active component and the zirconia as the carrier, and is a novel photocatalyst in which the zirconia carrier anchors the transition metal single atom. The carrier of the photocatalyst is zirconia with defect sites, and the existence of defect sites provides the possibility to achieve stable single-atom anchoring of transition metals. At the same time, the transition metal single atoms anchored by defect sites are not easy to agglomerate in catalytic applications due to the strong metal-support interaction, which can greatly improve their stability in photocatalytic reactions. In the application of the transition metal single-atom photocatalyst, by virtue of the special unsaturated coordination state of the transition metal single atom, high activity and high selectivity of gas-solid reduction of carbon dioxide to carbon monoxide can be achieved. Furthermore, the use of sacrificial agents to overcome the photooxidation/photocorrosion of this catalyst is avoided due to the stability of the defect site-anchored transition metal single atoms. Therefore, the preparation method is low in cost, simple in process, and full of prospects in practical applications.
本发明提供的过渡金属单原子催化剂的制备方法中,以锆、过渡金属胶状物为前驱体,通过低温、高温处理一步法实现了缺陷位氧化锆的制备以及在其表面锚定过渡金属单原子。且该制备方法具有普适性,可用于制备多种过渡金属单原子催化剂,通过该方法实现了Zn单原子催化剂,Fe单原子催化剂,Co单原子催化剂,Ni单原子催化剂,Cu单原子催化剂的制备。此外,该制备方法成本低廉、工艺简单、能够大规模生产。In the preparation method of the transition metal single-atom catalyst provided by the present invention, zirconium and transition metal colloid are used as precursors, and the preparation of defect site zirconia and the anchoring of transition metal single-atom on its surface are realized by a one-step method of low temperature and high temperature treatment. atom. And the preparation method is universal and can be used to prepare a variety of transition metal single-atom catalysts. Through this method, Zn single-atom catalysts, Fe single-atom catalysts, Co single-atom catalysts, Ni single-atom catalysts, and Cu single-atom catalysts are realized. preparation. In addition, the preparation method has the advantages of low cost, simple process and large-scale production.
本发明提供的该催化剂在光催化二氧化碳还原制备一氧化碳的应用中,具有较高的一氧化碳产物选择性和生成活性。The catalyst provided by the invention has high carbon monoxide product selectivity and generation activity in the application of photocatalytic reduction of carbon dioxide to prepare carbon monoxide.
附图说明Description of drawings
下面结合附图对本发明的具体实施方式作进一步详细的说明。The specific embodiments of the present invention will be described in further detail below with reference to the accompanying drawings.
图1示出本发明实施例1所获得的Ni单原子催化剂的XRD谱图。FIG. 1 shows the XRD pattern of the Ni single-atom catalyst obtained in Example 1 of the present invention.
图2示出本发明实施例1所获得的Ni单原子催化剂的EPR图。FIG. 2 shows the EPR diagram of the Ni single-atom catalyst obtained in Example 1 of the present invention.
图3示出本发明实施例1所获得的缺陷位氧化锆的EPR图。FIG. 3 shows the EPR diagram of the defective zirconia obtained in Example 1 of the present invention.
图4示出本发明实施例1所获得的Ni单原子催化剂的TEM图。FIG. 4 shows the TEM image of the Ni single-atom catalyst obtained in Example 1 of the present invention.
图5示出本发明实施例1所获得的Ni单原子催化剂的HAADF-STEM图。FIG. 5 shows the HAADF-STEM image of the Ni single-atom catalyst obtained in Example 1 of the present invention.
图6示出本发明实施例1所获得的Ni单原子催化剂的光催化二氧化碳还原性能图。FIG. 6 is a graph showing the photocatalytic carbon dioxide reduction performance of the Ni single-atom catalyst obtained in Example 1 of the present invention.
图7示出实施例2-4所合成的Ni单原子催化剂的XRD图。FIG. 7 shows the XRD patterns of the Ni single-atom catalysts synthesized in Examples 2-4.
图8示出本发明实施例2-4所获得的Ni单原子催化剂的光催化二氧化碳还原性能图。FIG. 8 is a graph showing the photocatalytic carbon dioxide reduction performance of the Ni single-atom catalysts obtained in Examples 2-4 of the present invention.
图9示出实施例1和实施例5中所合成的Ni单原子XRD图。FIG. 9 shows Ni single-atom XRD patterns synthesized in Example 1 and Example 5. FIG.
图10示出本发明实施例5所获得的Ni单原子催化剂的光催化二氧化碳还原性能图。FIG. 10 is a graph showing the photocatalytic carbon dioxide reduction performance of the Ni single-atom catalyst obtained in Example 5 of the present invention.
图11示出实施例6中所合成的单原子催化剂的XRD图。FIG. 11 shows the XRD pattern of the single-atom catalyst synthesized in Example 6. FIG.
图12示出本发明实施例6、7所获得的Ni单原子催化剂的光催化二氧化碳还原性能图。FIG. 12 is a graph showing the photocatalytic carbon dioxide reduction performance of the Ni single-atom catalysts obtained in Examples 6 and 7 of the present invention.
图13示出实施例8-11中得到的Cu、Zn、Fe、Co单原子催化剂的球差校正透射电镜图。图14示出实施例8-11中得到的单原子催化剂的XRD图。FIG. 13 shows the spherical aberration-corrected transmission electron microscope images of the Cu, Zn, Fe, Co single-atom catalysts obtained in Examples 8-11. 14 shows the XRD patterns of the single-atom catalysts obtained in Examples 8-11.
图15示出本发明实施例8-11所获得的Ni单原子催化剂的光催化二氧化碳还原性能图。FIG. 15 shows the photocatalytic carbon dioxide reduction performance of the Ni single-atom catalysts obtained in Examples 8-11 of the present invention.
图16示出对比例1所获得的Ni单原子催化剂的XRD图。FIG. 16 shows the XRD pattern of the Ni single-atom catalyst obtained in Comparative Example 1. FIG.
图17示出对比例2所获得的催化剂的XRD图。FIG. 17 shows the XRD pattern of the catalyst obtained in Comparative Example 2. FIG.
具体实施方式Detailed ways
为了更清楚地说明本发明,下面结合优选实施例和附图对本发明做进一步的说明。附图中相似的部件以相同的附图标记进行表示。本领域技术人员应当理解,下面所具体描述的内容是说明性的而非限制性的,不应以此限制本发明的保护范围。In order to illustrate the present invention more clearly, the present invention will be further described below with reference to the preferred embodiments and accompanying drawings. Similar parts in the figures are denoted by the same reference numerals. Those skilled in the art should understand that the content specifically described below is illustrative rather than restrictive, and should not limit the protection scope of the present invention.
实施例1Example 1
一种氧化锆锚定过渡金属Ni单原子光催化剂的方法,包括如下步骤:A method for zirconia anchoring transition metal Ni single-atom photocatalyst, comprising the steps of:
1)称取0.53mmol硝酸镍,6.75mmol硝酸锆加入烧杯中,加入100mL去离子水,磁力搅拌至完全溶解得到澄清透明的溶液;此步骤中不加入硝酸镍时在制备结束后得到具有缺陷位的氧化锆;1) take by weighing 0.53mmol nickel nitrate, 6.75mmol zirconium nitrate is added in the beaker, add 100mL deionized water, magnetically stir to completely dissolve to obtain a clear and transparent solution; when not adding nickel nitrate in this step, obtain a defective position after the preparation is completed. zirconia;
2)待反应完成后,称取15mmol(NH4)2CO3于100mL去离子水彻底溶解,后加入上述得到的澄清透明的溶液,出现絮状产物;2) After the reaction is completed, take 15mmol (NH 4 ) 2 CO 3 and dissolve it in 100 mL of deionized water thoroughly, then add the clear and transparent solution obtained above, and a flocculent product appears;
3)上述得到的絮状产物在70℃水浴条件下持续搅拌5h,最终得到凝胶状产物;3) The flocculent product obtained above was continuously stirred for 5 hours under the condition of a 70°C water bath, and finally a gel-like product was obtained;
4)上述得到的凝胶状产物在空气气氛下以5℃·min-1升温速率升温到600℃,在该温度下保持2h,完毕后自然降温到室温,得到粉末状产物;4) The gel-like product obtained above was heated to 600° C. at a heating rate of 5° C. min −1 in an air atmosphere, kept at this temperature for 2 h, and then cooled down to room temperature naturally to obtain a powdery product;
5)上述得到的粉末状产物分别使用稀盐酸和去离子水洗涤各三次,直到洗涤液倒出时完全无色透明时,离心并在60℃烘箱中烘干2h,即得到Ni单原子催化剂,记为Ni-SAC,通过ICP-AES方法,可以检测到该Ni-SAC中,Ni原子的负载量为1.8wt%。5) The powdered product obtained above was washed three times with dilute hydrochloric acid and deionized water respectively, until the washing liquid was completely colorless and transparent when poured out, centrifuged and dried in an oven at 60°C for 2 hours to obtain a Ni single-atom catalyst, It is denoted as Ni-SAC, and it can be detected by ICP-AES method that the loading amount of Ni atoms in this Ni-SAC is 1.8 wt%.
该催化剂的XRD谱图、缺陷位氧化锆的EPR图、该催化剂的EPR图、TEM图、HAADF-STEM图依次如图1-5所示。The XRD pattern of the catalyst, the EPR pattern of the defective zirconia, the EPR pattern of the catalyst, the TEM pattern, and the HAADF-STEM pattern are sequentially shown in Figures 1-5.
将所述催化剂用于光催化二氧化碳还原制备一氧化碳中:The catalyst is used in photocatalytic reduction of carbon dioxide to prepare carbon monoxide:
在0.08Mpa压力下,将50mL CO2和水蒸气的混合气,10mg上述催化剂,采用全太阳光谱光照2h,采用气相色谱外标的方法测试得到的产物的产率等。图6示出本发明实施例1所获得的Ni单原子催化剂的光催化二氧化碳还原性能图。由图中可以看出,实施例1所获得的Ni单原子催化剂在光催化CO2还原后得到CO,CO的生成速率为11.8μmol/g·h,CO的产物选择性为92.5%(其余为H2的选择性)。Under the pressure of 0.08Mpa, the mixture of 50mL CO 2 and water vapor, 10mg of the above catalyst, using full solar spectrum illumination for 2h, using gas chromatography external standard method to test the yield of the obtained product, etc. FIG. 6 is a graph showing the photocatalytic carbon dioxide reduction performance of the Ni single-atom catalyst obtained in Example 1 of the present invention. It can be seen from the figure that the Ni single-atom catalyst obtained in Example 1 obtains CO after photocatalytic CO reduction, the formation rate of CO is 11.8 μmol/g h, and the product selectivity of CO is 92.5% (the rest are selectivity of H2 ).
实施例2-4Example 2-4
重复实施例1,其区别仅在于将硝酸镍改为氯化镍、乙酸镍、硫酸镍。得到的Ni单原子催化剂与实施例1得到的单原子催化剂并无明显区别,且通过ICP-AES方法,可以检测到该Ni-SAC中,Ni原子的负载量为3wt%。Example 1 was repeated, except that nickel nitrate was changed to nickel chloride, nickel acetate, and nickel sulfate. There is no obvious difference between the obtained Ni single-atom catalyst and the single-atom catalyst obtained in Example 1, and through the ICP-AES method, it can be detected that in the Ni-SAC, the loading amount of Ni atoms is 3wt%.
图7为实施例2-4所合成的Ni单原子催化剂的XRD图,由图中可以看出,采用氯化镍、乙酸镍、硫酸镍所合成的Ni单原子催化剂均只出现氧化锆的峰,并未出现Ni或其化合物的峰。这也说明,过渡金属盐中阴离子种类对形成单原子催化剂没有明显影响。Fig. 7 is the XRD pattern of the Ni single-atom catalyst synthesized by embodiment 2-4, as can be seen from the figure, the Ni single-atom catalyst synthesized by using nickel chloride, nickel acetate, nickel sulfate all only appears the peak of zirconia , there is no peak of Ni or its compounds. This also shows that the anion species in the transition metal salt has no obvious effect on the formation of single-atom catalysts.
将实施例2-4制备得到的催化剂用于光催化二氧化碳还原制备一氧化碳中:The catalyst prepared in Example 2-4 was used in the photocatalytic reduction of carbon dioxide to prepare carbon monoxide:
在0.08Mpa压力下,将10mL CO2和水蒸气的混合气,50mg上述催化剂,采用全太阳光谱光照5h,采用气相色谱外标的方法测试得到的产物的产率等。Under the pressure of 0.08Mpa, the mixture of 10mL CO 2 and water vapor, 50mg of the above catalyst, using full solar spectrum illumination for 5h, using gas chromatography external standard method to test the yield of the obtained product, etc.
图8示出本发明实施例2-4所获得的Ni单原子催化剂的光催化二氧化碳还原性能图。由图中可以看出,实施例2-4所获得的Ni单原子催化剂在光催化CO2还原后得到CO,CO的生成速率分别为5.2μmol/g·h,6.1μmol/g·h,3.4μmol/g·h;CO的产物选择性分别为95.2%,90.3%,98.4%(其余为H2的选择性)。FIG. 8 is a graph showing the photocatalytic carbon dioxide reduction performance of the Ni single-atom catalysts obtained in Examples 2-4 of the present invention. It can be seen from the figure that the Ni single-atom catalysts obtained in Examples 2-4 obtained CO after photocatalytic CO reduction, and the formation rates of CO were 5.2 μmol/g·h, 6.1 μmol/g·h, 3.4 μmol/g·h, respectively. μmol/g·h; the product selectivities of CO were 95.2%, 90.3%, and 98.4%, respectively (the remainder was the selectivity of H2 ).
实施例5Example 5
重复实施例1,其区别仅在于将硝酸锆改为乙酸锆,得到的催化剂为单原子催化剂,且通过ICP-AES方法,可以检测到该Ni-SAC中,Ni原子的负载量为2wt%。Example 1 was repeated, except that the zirconium nitrate was changed to zirconium acetate, the obtained catalyst was a single-atom catalyst, and by ICP-AES method, it could be detected that in the Ni-SAC, the loading amount of Ni atoms was 2wt%.
图9所示为实施例1和实施例5中所合成的Ni单原子XRD图。图中,所合成的Ni单原子均只有氧化锆的峰出现,没有出现金属单质或化合物的峰。这说明锆盐类型对形成单原子催化剂没有明显影响。9 shows the Ni single-atom XRD patterns synthesized in Example 1 and Example 5. In the figure, for the synthesized Ni single atoms, only the peak of zirconia appears, and there is no peak of metal element or compound. This indicates that the type of zirconium salt has no significant effect on the formation of single-atom catalysts.
将实施例5制备得到的催化剂用于光催化二氧化碳还原制备一氧化碳中:The catalyst prepared in Example 5 was used in the photocatalytic reduction of carbon dioxide to prepare carbon monoxide:
在0.05Mpa压力下,将100mL CO2和水蒸气的混合气,100mg上述催化剂,采用全太阳光谱光照2h,采用气相色谱外标的方法测试得到的产物的产率等。Under the pressure of 0.05Mpa, the mixture of 100mL CO 2 and water vapor, 100mg of the above catalyst, and the full solar spectrum illumination for 2h were used to test the yield of the obtained product by gas chromatography external standard method.
图10示出本发明实施例5所获得的Ni单原子催化剂的光催化二氧化碳还原性能图。由图中可以看出,实施例5所获得的Ni单原子催化剂在光催化CO2还原后得到CO,CO的生成速率为9.5μmol/g·h,CO的产物选择性为88.4%(其余为H2的选择性)。FIG. 10 is a graph showing the photocatalytic carbon dioxide reduction performance of the Ni single-atom catalyst obtained in Example 5 of the present invention. It can be seen from the figure that the Ni single-atom catalyst obtained in Example 5 obtained CO after photocatalytic CO reduction, the formation rate of CO was 9.5 μmol/g h, and the product selectivity of CO was 88.4% (the rest were selectivity of H2 ).
实施例6-7Example 6-7
重复实施例1,其区别仅在于将(NH4)2CO3加入量改为20mmol和30mmol,得到的催化剂记为NiN20和NiN30,所合成的两种催化剂均为单原子催化剂。Example 1 was repeated, except that the addition amount of (NH 4 ) 2 CO 3 was changed to 20 mmol and 30 mmol, the obtained catalysts were denoted as NiN20 and NiN30, and the two synthesized catalysts were single-atom catalysts.
图11示出实施例6中所合成的单原子催化剂的XRD图。图中仅出现两个对应氧化锆的宽峰,没有金属或其化合物的峰出现,这说明所合成的两种催化剂均为单原子催化剂。FIG. 11 shows the XRD pattern of the single-atom catalyst synthesized in Example 6. FIG. There are only two broad peaks corresponding to zirconia in the figure, and no peaks of metals or their compounds appear, which indicates that the two synthesized catalysts are single-atom catalysts.
将实施例6-7制备得到的催化剂用于光催化二氧化碳还原制备一氧化碳中:The catalysts prepared in Examples 6-7 were used in the photocatalytic reduction of carbon dioxide to prepare carbon monoxide:
在0.01Mpa压力下,将100mL CO2和水蒸气的混合气,50mg上述催化剂,采用全太阳光谱光照5h,采用气相色谱外标的方法测试得到的产物的产率等。Under the pressure of 0.01Mpa, the mixture of 100mL CO 2 and water vapor, 50mg of the above catalyst, using full solar spectrum illumination for 5h, using gas chromatography external standard method to test the yield of the obtained product, etc.
图12示出本发明实施例6-7所获得的Ni单原子催化剂的光催化二氧化碳还原性能图。由图中可以看出,实施例6-7所获得的Ni单原子催化剂在光催化CO2还原后得到CO,CO的生成速率分别为3.2μmol/g·h,4.4μmol/g·h;CO的产物选择性分别为60.9%,54.2%(其余为H2的选择性)。FIG. 12 shows the photocatalytic carbon dioxide reduction performance diagram of the Ni single-atom catalysts obtained in Examples 6-7 of the present invention. It can be seen from the figure that the Ni single-atom catalysts obtained in Examples 6-7 obtained CO after photocatalytic CO reduction, and the formation rates of CO were 3.2 μmol/g·h and 4.4 μmol/g·h, respectively; CO The product selectivities were 60.9% and 54.2%, respectively (the remainder was the selectivity of H2 ).
实施例8-11Examples 8-11
重复实施例1,其区别仅在于将金属盐改为Cu、Zn、Fe、Co盐。所得到的催化剂均为单原子催化剂。具体地,这4种金属单原子催化剂的球差校正透射电镜图如图13所示,标记暗点为金属单原子。可以发现过渡金属都是以单原子形式分散在氧化锆的表面和内部。其对应的XRD图如图14所示,只有氧化锆的峰出现,没有出现金属单质或化合物的峰。实施例8-11,也说明该过渡金属单原子催化剂合成方法具有广泛的普适性。Example 1 was repeated, except that the metal salts were changed to Cu, Zn, Fe, Co salts. The obtained catalysts are all single-atom catalysts. Specifically, the spherical aberration-corrected transmission electron microscope images of the four metal single-atom catalysts are shown in Figure 13, and the marked dark spots are metal single atoms. It can be found that the transition metals are dispersed on the surface and inside of zirconia in the form of single atoms. The corresponding XRD pattern is shown in FIG. 14 , only the peak of zirconia appears, and the peak of metal element or compound does not appear. Examples 8-11 also illustrate that the synthesis method of the transition metal single-atom catalyst has wide applicability.
将实施例8-11制备得到的催化剂用于光催化二氧化碳还原制备一氧化碳中:The catalysts prepared in Examples 8-11 were used in photocatalytic reduction of carbon dioxide to prepare carbon monoxide:
在0.08Mpa压力下,将40mL CO2和水蒸气的混合气,10mg上述催化剂,采用全太阳光谱光照4h,采用气相色谱外标的方法测试得到的产物的产率等。Under the pressure of 0.08Mpa, the mixture of 40mL CO 2 and water vapor, 10mg of the above catalyst, using full solar spectrum illumination for 4h, using gas chromatography external standard method to test the yield of the obtained product, etc.
图15示出本发明实施例8-11所获得的Ni单原子催化剂的光催化二氧化碳还原性能图。由图中可以看出,实施例8-11所获得的Ni单原子催化剂在光催化CO2还原后得到CO,CO的生成速率分别为8.8μmol/g·h,10.4μmol/g·h,6.5μmol/g·h,9.2μmol/g·h;CO的产物选择性分别为87.1%,91.5%,60.5%,72.3%(其余为H2的选择性)。FIG. 15 shows the photocatalytic carbon dioxide reduction performance of the Ni single-atom catalysts obtained in Examples 8-11 of the present invention. It can be seen from the figure that the Ni single-atom catalysts obtained in Examples 8-11 obtained CO after photocatalytic CO reduction, and the formation rates of CO were 8.8 μmol/g·h, 10.4 μmol/g·h, 6.5 μmol/g·h, respectively. μmol/g·h, 9.2 μmol/g·h; the product selectivities of CO were 87.1%, 91.5%, 60.5%, 72.3%, respectively (the remainder was the selectivity of H2 ).
对比例1Comparative Example 1
重复实施例1,其区别仅在于将硝酸锆改为硝酸铈。所得到的催化剂均能够形成单原子催化剂。通过ICP-AES测试得到其负载量仅为0.5wt%。Example 1 was repeated except that the zirconium nitrate was changed to cerium nitrate. The resulting catalysts were all capable of forming single-atom catalysts. Through the ICP-AES test, its loading was only 0.5 wt%.
图16示出本发明对比例1所获得的的Ni单原子催化剂的XRD图。可以看出只有氧化铈的峰出现,而无Ni金属单质或化合物的峰。FIG. 16 shows the XRD pattern of the Ni single-atom catalyst obtained in Comparative Example 1 of the present invention. It can be seen that only the peak of cerium oxide appears, and there is no peak of Ni metal element or compound.
对比例2Comparative Example 2
重复实施例1,其区别仅在于将硝酸锆改为四氯化钛。所得到的催化剂均能够形成单原子催化剂。Example 1 was repeated except that the zirconium nitrate was changed to titanium tetrachloride. The resulting catalysts were all capable of forming single-atom catalysts.
图17示出本发明对比例1所获得的的Ni单原子催化剂的XRD图。可以看出只有氧化钛的峰出现,而无Ni金属单质或化合物的峰。FIG. 17 shows the XRD pattern of the Ni single-atom catalyst obtained in Comparative Example 1 of the present invention. It can be seen that only the peak of titanium oxide appears, and there is no peak of Ni metal element or compound.
对比例3Comparative Example 3
重复实施例6,区别在于,将步骤4)中升温速率改为1℃·min-1,其余条件不变,制备得到催化剂。Example 6 was repeated, except that the temperature increase rate in step 4) was changed to 1°C·min −1 , and the other conditions remained unchanged to prepare a catalyst.
采用如实施例6的应用条件将所述催化剂用于光催化二氧化碳还原制备一氧化碳中,结果:CO的生成速率为2.7μmol/g·h,CO的产物选择性为50.1%(其余为H2的选择性)。The catalyst was used in the photocatalytic reduction of carbon dioxide to prepare carbon monoxide using the application conditions as in Example 6. The results showed that the formation rate of CO was 2.7 μmol/g·h, and the product selectivity of CO was 50.1% (the rest was H2 optional).
对比例4Comparative Example 4
重复实施例6,区别在于,将步骤4)中升温速率改为12℃·min-1,其余条件不变,制备得到催化剂。Example 6 was repeated, except that the temperature increase rate in step 4) was changed to 12°C·min −1 , and the other conditions remained unchanged to prepare the catalyst.
采用如实施例6的应用条件将所述催化剂用于光催化二氧化碳还原制备一氧化碳中,结果:CO的生成速率为2.6μmol/g·h,CO的产物选择性为51.3%(其余为H2的选择性)。The catalyst was used in the photocatalytic reduction of carbon dioxide to prepare carbon monoxide using the application conditions as in Example 6. The results showed that the formation rate of CO was 2.6 μmol/g·h, and the product selectivity of CO was 51.3% (the rest was H2 optional).
显然,本发明的上述实施例仅仅是为清楚地说明本发明所作的举例,而并非是对本发明的实施方式的限定,对于所属领域的普通技术人员来说,在上述说明的基础上还可以做出其它不同形式的变化或变动,这里无法对所有的实施方式予以穷举,凡是属于本发明的技术方案所引伸出的显而易见的变化或变动仍处于本发明的保护范围之列。Obviously, the above-mentioned embodiments of the present invention are only examples for clearly illustrating the present invention, rather than limiting the embodiments of the present invention. Changes or changes in other different forms cannot be exhausted here, and all obvious changes or changes derived from the technical solutions of the present invention are still within the protection scope of the present invention.
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CN116371412A (en) * | 2023-02-20 | 2023-07-04 | 天津大学 | A method for regulating the size of Cu atomic clusters in copper-based catalysts |
Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN103756397A (en) * | 2013-12-27 | 2014-04-30 | 淄博广通化工有限责任公司 | Zirconia composite nano-powder material and preparation method thereof |
CN105056952A (en) * | 2015-08-19 | 2015-11-18 | 中国科学院理化技术研究所 | Preparation method and application of nickel-based photocatalyst for preparing high-carbon hydrocarbon above carbon dioxide by photocatalytic carbon monoxide hydrogenation |
CN110479249A (en) * | 2019-08-19 | 2019-11-22 | 中山大学 | A kind of method that presoma atomization prepares monatomic catalyst |
CN111514893A (en) * | 2020-04-17 | 2020-08-11 | 中国科学院合肥物质科学研究院 | Catalyst with sub-nanometer composite structure and preparation method thereof |
CN111530458A (en) * | 2020-05-15 | 2020-08-14 | 江南大学 | A single-atom catalyst and its application in carbon dioxide hydrogenation |
-
2020
- 2020-12-01 CN CN202011384868.8A patent/CN114570344A/en active Pending
Patent Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN103756397A (en) * | 2013-12-27 | 2014-04-30 | 淄博广通化工有限责任公司 | Zirconia composite nano-powder material and preparation method thereof |
CN105056952A (en) * | 2015-08-19 | 2015-11-18 | 中国科学院理化技术研究所 | Preparation method and application of nickel-based photocatalyst for preparing high-carbon hydrocarbon above carbon dioxide by photocatalytic carbon monoxide hydrogenation |
CN110479249A (en) * | 2019-08-19 | 2019-11-22 | 中山大学 | A kind of method that presoma atomization prepares monatomic catalyst |
CN111514893A (en) * | 2020-04-17 | 2020-08-11 | 中国科学院合肥物质科学研究院 | Catalyst with sub-nanometer composite structure and preparation method thereof |
CN111530458A (en) * | 2020-05-15 | 2020-08-14 | 江南大学 | A single-atom catalyst and its application in carbon dioxide hydrogenation |
Non-Patent Citations (1)
Title |
---|
XUYANG XIONG等: ""Photocatalytic CO2 Reduction to CO over Ni Single Atoms Supported on Defect-Rich Zirconia"", ADV. ENERGY MATER., vol. 10, no. 46, pages 1 - 8 * |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN116371412A (en) * | 2023-02-20 | 2023-07-04 | 天津大学 | A method for regulating the size of Cu atomic clusters in copper-based catalysts |
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