CN110931804A - CeO carried by Pt-Ni-Cu ternary alloy2Preparation of composite material and research on formic acid catalytic performance of composite material - Google Patents

Abstract

The invention relates to a Pt-Ni-Cu ternary alloy supported CeO₂Preparation and catalytic performance study. The invention utilizes a microwave thermal method to synthesize Pt-Ni-Cu ternary metal alloy supported cerium dioxide nano particles in one step, and specifically, CeO can be prepared by adding formaldehyde₂Inducing the surface gap in the forming process of the concave octahedron Pt-Ni-Cu alloy, keeping the shape of the Pt-Ni-Cu ternary metal in the process, ensuring that the obtained nano particle continuously shows excellent specific area activity in formic acid electrooxidation, fully ensuring the utilization efficiency of metal atoms, surprisingly finding that the particle size is obviously larger than that of a commercial Pt catalyst, also achieving higher specific quality activity than that of the commercial catalyst, obviously improving the catalytic utilization efficiency of noble metal, and achieving the aim of pre-preparing the Pt-Ni-Cu ternary metalThe technical effect that the material cannot be obtained can further improve the anti-poisoning capability and the electrocatalytic stability of the catalysis of the prepared metal alloy.

Description

CeO carried by Pt-Ni-Cu ternary alloy2Preparation of composite material and research on formic acid catalytic performance thereofIs especially suitable for the treatment of diabetes

Technical Field

The invention belongs to the field of functional composite nano materials. Specifically, the invention relates to an alloy supported CeO₂Preparation and application of functional material.

Background

Currently, proton membrane fuel cells have become a highly efficient energy supply for automobiles and other portable devices. The Pt-based catalyst in PEMFCs remains the best catalyst, but the expensive price of metallic platinum is a major reason why it is difficult to industrially produce proton membrane fuel cells on a large scale. Therefore, metals of other transition elements are added to form binary or ternary metal alloys to reduce oxygen adsorption bond energy and reduce cost, for example, PtCuNi ternary alloys are prepared by regulating morphology to improve electrocatalytic performance and stability in patent document CN110380068A, but the problems of high catalyst cost, low actual utilization efficiency of precious metals and the like are still faced.

In a fuel cell, a platinum-based catalyst mainly catalyzes an organic fuel to help the organic fuel react. Because organic fuel contains a large amount of C element, the prepared platinum-based catalyst inevitably generates little CO in the process of catalytic oxidation, and the generated CO is attached to the surface of the catalyst, thereby occupying the active site of the catalyst and influencing the catalytic activity, which is the phenomenon known as catalyst poisoning. However, when the platinum-based ternary alloy catalyst is applied to the anode material of the proton exchange membrane fuel cell at present, the poisoning resistance of the commonly prepared platinum-based ternary alloy catalyst material is poor.

CeO₂Having relatively stable positive tetravalent cerium ions, CeO being known₂The catalyst can be used for catalyzing and oxidizing CO. However, by CeO alone₂As fuel cell catalysts, the oxidation activity is poor, in which case one may choose to add some noble metals like Pt to increase CeO₂The oxidation activity of (3). However, in the noble metal composite catalyst material, the most important key is the interaction between the support and the noble metal. The existence state and dispersion degree of the noble metal influence the activity of the catalyst material, and the noble metal and the carrier are researchedThe interaction mode between the two has important significance for the research and development and application of the catalyst material.

Disclosure of Invention

Aiming at the technical problems, the invention solves the technical problems of low unit mass utilization efficiency, easy poisoning and the like of the existing Pt nano-structured catalyst, and prepares a Pt-Ni-Cu ternary alloy supported CeO₂The preparation method improves the performance of the Pt-based nano-structure catalyst.

In order to achieve the purpose, the invention is realized by the following technical scheme.

CeO supported by Pt-Ni-Cu ternary alloy₂The experimental procedure of the preparation method of (1) is as follows:

(1) 1 mL of oleylamine corresponded to 3.44 mg of CeO₂Fully performing ultrasonic dispersion on the original solution, respectively putting 0.05-0.3 mL of the original solution into a centrifuge tube, centrifuging, sucking supernatant liquid by using a liquid-transferring gun until only precipitate is left, and adding 0.7mL of ethanolamine for ultrasonic dispersion to uniformly disperse the supernatant liquid;

(2) 303.4 mg of glycine, 200 mg of polyvinylpyrrolidone (PVP) and 300 mg of sodium iodide are respectively weighed in a clean beaker;

(3) 2 mL of 20 mM H were added in sequence₂PtCl₆Aqueous solution, 1 mL of 20 mM CuCl₂Aqueous solution, 1 mL of 20 mM NiCl₂Adding the aqueous solution into the beaker of the sample in the step (2), and adding the fully dispersed CeO-containing solution₂Adding the ethanolamine into the beaker, stirring for 24 hours until the solution is blue and transparent, transferring 600 mu L (40%) of formaldehyde solution, slowly dropwise adding the formaldehyde solution into the beaker, and continuously stirring for 15 min;

(4) putting the fully stirred solution in the step (3) into a microwave reaction kettle, and preserving the heat for 30 min at 200 ℃;

(5) fully ultrasonically treating the solution in the kettle, transferring the solution into a centrifugal tube, centrifuging once at 10000 r/min for 15 min, pouring out the supernatant, adding water and ethanol into the centrifugal tube at a ratio of 1:1, ultrasonically treating the solution to ensure that the obtained precipitate is fully and uniformly dispersed, washing the precipitate for three times at 10000 r/min for 15 min, adding 1 mL of n-butylamine into the washed precipitate, ultrasonically treating the precipitate, and soaking the precipitate for one day;

(7) centrifuging the sample soaked with n-butylamine for one day at 10000 r/min for 15 min, pouring out the supernatant, adding water and ethanol 1:1 into a centrifugal tube, performing ultrasonic treatment, centrifuging at 10000 r/min for 15 min, washing for several times, and freeze-drying.

The invention has the beneficial effects that: (1) different from the traditional research method in CeO₂Carrying noble metals or CeO₂Simply compounding with noble metal, and synthesizing the CeO with very small diameter by utilizing the gap in forming the concave octahedron Pt-Ni-Cu alloy group₂Adding to the surface of the catalyst with CeO₂The strong oxidation effect on CO is used for improving the CO poisoning resistance of the metal catalyst and improving the electrocatalytic stability of the metal catalyst.

(2) The method is characterized in that Pt-Ni-Cu ternary metal alloy supported cerium dioxide nano particles are synthesized in one step by a microwave thermal method, and specifically, CeO can be prepared by adding formaldehyde₂Inducing voids on the surface during the formation of the concave octahedral Pt-Ni-Cu alloy. The content of cerium dioxide added in each sample is changed, the optimal cerium dioxide loading amount is obtained through result comparison, the morphology of Pt-Ni-Cu ternary metal is maintained in the process, the obtained nanoparticles continuously show excellent specific area activity in formic acid electrooxidation, the utilization efficiency of metal atoms is fully guaranteed, and surprisingly, on the basis that the particle size is remarkably larger than that of a commercial Pt catalyst, higher specific quality activity than that of the commercial catalyst can be achieved, the precious metal catalytic utilization efficiency is remarkably improved, an unexpected technical effect is achieved, and the poisoning resistance of the prepared metal alloy catalyst can be further improved.

Drawings

FIG. 1 is a TEM image of a catalyst obtained by adding CeO2 in various amounts.

FIG. 2 shows the results of the preparation of the different catalysts of example 1 at 0.25M HCOOH + 0.5M H₂SO₄The specific area activity obtained in the solution.

FIG. 3 shows the results of the preparation of the different catalysts of example 1 at 0.25M HCOOH + 0.5M H₂SO₄Specific mass activity obtained in solution.

FIG. 4 is a plot of the chronoamperometric current of a formic acid fuel cell at a constant potential of 0.06V for the different catalysts prepared in example 1.

FIG. 5 is a graphical representation of the CO poisoning resistance of various catalysts prepared in example 1.

Detailed Description

The following examples are intended to illustrate the practice and advantageous effects of the present invention, but are not to be construed as limiting the scope of the present invention.

Example 1

CeO supported by Pt-Ni-Cu ternary alloy₂The experimental procedure of the preparation method of (1) is as follows:

(1) fully ultrasonically dispersing 1 mL of crude solution of oleylamine corresponding to 3.44 mg of CeO2, respectively adding (a) 0 mL (b) 0.07mL (c) 0.2 mL and (d) 0.3 mL into a centrifuge tube, centrifuging, sucking supernatant liquid by using a pipette until only precipitate is remained, and adding 0.7mL of ethanolamine for ultrasonic dispersion to uniformly disperse;

(2) 303.4 mg of glycine, 200 mg of polyvinylpyrrolidone (PVP) and 300 mg of sodium iodide are respectively weighed in a clean beaker;

(3) 2 mL of 20 mM H were added in sequence₂PtCl₆Aqueous solution, 1 mL of 20 mM CuCl₂Aqueous solution, 1 mL of 20 mM NiCl₂Adding the aqueous solution into the beaker of the sample in the step (2), and adding the fully dispersed CeO-containing solution₂Adding the ethanolamine into the beaker, stirring for 24 hours until the solution is blue and transparent, transferring 600 mu L (40%) of formaldehyde solution, slowly dropwise adding the formaldehyde solution into the beaker, and continuously stirring for 15 min;

(4) putting the fully stirred solution in the step (3) into a microwave reaction kettle, and preserving the heat for 30 min at 200 ℃;

(5) fully ultrasonically treating the solution in the kettle, transferring the solution into a centrifugal tube, centrifuging once at 10000 r/min for 15 min, pouring out the supernatant, adding water and ethanol into the centrifugal tube at a ratio of 1:1, ultrasonically treating the solution to ensure that the obtained precipitate is fully and uniformly dispersed, washing the precipitate for three times at 10000 r/min for 15 min, adding 1 mL of n-butylamine into the washed precipitate, ultrasonically treating the precipitate, and soaking the precipitate for one day;

(7) centrifuging the sample soaked with n-butylamine for one day at 10000 r/min for 15 min, pouring out the supernatant, adding water and ethanol 1:1 into a centrifugal tube, performing ultrasonic treatment, centrifuging at 10000 r/min for 15 min, washing for several times, and freeze-drying to obtain a product TEM as shown in figure 1.

As can be seen from FIG. 1, with CeO₂The ceO added into the original Pt-Ni-Cu ternary alloy with the concave hollow structure is added continuously₂The filling can ensure the CeO₂Less active sites of Pt are occupied, and CeO can be ensured in the catalytic reaction₂The provided hydroxyl group can promote deprotonation and dehydrogenation in the oxidation reaction, so that the CO poisoning resistance is improved, and the stability of the catalyst is further improved. And further carrying out catalytic performance research on the catalyst, wherein the specific research method is as follows.

We used a three-electrode system to perform electrochemical catalytic tests on a CHI760e type electrochemical workstation, with a saturated calomel electrode (SCE in saturated KCl solution) as a reference electrode, a Pt wire electrode as a counter electrode, and a glassy carbon electrode (GC) as a working electrode. The use method of the GC electrode comprises the following steps: using Al with diameter of 1 μm, 0.3 μm and 0.05 μm before each use₂O₃Polishing the powder into a mirror surface, ultrasonically washing the mirror surface with ethanol for two to three times, and drying the mirror surface with an infrared drying oven. And (3) GC electrode dropwise adding: and transferring 6 muL of catalyst suspension under the drying treatment of an infrared lamp, dripping the catalyst suspension onto the surface of the GC electrode, dripping 2 muL of 0.5 wt% Nafion solution onto the surface of the working electrode, and drying the surface of the GC electrode under the infrared drying.

Electrochemical activation area test: at 0.5M H₂SO₄Taking the solution as an electrolyte solution, introducing high-purity N₂And removing dissolved oxygen from the electrolyte, and then performing Cyclic Voltammetry (CV) scanning at a scanning rate of 50 mV/s in a scanning range of-0.24-1.0V. An inert gas was maintained above the solution during the experiment. Until the last turn coincides with the penultimate turn. Formic acid electrooxidation test: at a concentration of 0.25M HCOOH + 0.5M H₂SO₄Is carried out under the electrolyte and high-purity N is introduced₂Removal of dissolved oxygen from electrolytesAnd then, performing CV scanning with the scanning speed of 50 mV/s and the scanning range of-0.24-1.0V. Keeping inert gas above the solution in the process until the final two circles of superposition are finished.

As can be seen from fig. 2, we normalized the positive sweep to ECSA and observed that the resulting current density was high and low, and thus the magnitude of the catalyst activity. We see that 0.07mL of CeO was added₂The catalyst of (3) has the highest activity. Description with CeO₂The electrocatalytic activity of formic acid increases first and then decreases, and a large amount of CeO is shown in a TEM image₂Occupying the surface of the catalyst, can prevent the catalyst from contacting with the solution in the catalysis process and further influence the electrocatalytic performance of the catalyst.

The specific mass activity is expressed as the current density I/(mA/mg) produced per unit mass of the catalyst^-1) The specific mass activity was evaluated based on the total amount of the catalyst dropped on the surface of the platinum-carbon electrode. It has a large relationship with the Pt content of the catalyst. When we explore the electrocatalytic performance of the catalyst, not only the area specific activity diagram is needed, but also the mass specific activity plays an important role in exploring the electrocatalytic performance of the catalyst. Observation of FIG. 3 We know that 0.07mL of CeO was added₂Compared with other catalysts, the catalyst has higher catalytic activity, the Pt-Ni-Cu ternary alloy catalyst with higher area specific activity has relatively lower mass specific activity, and the surface is loaded with CeO₂The catalyst of (3) has a higher atom utilization efficiency than the unsupported alloy catalyst.

Time current curve: at 0.25M HCOOH + 0.5M H₂SO₄The voltage of the sweep timing current curve is 0.06V, the test time is 1000 s, and the stability of the catalyst is better than that of the commercial platinum catalyst according to the graph shown in FIG. 4. Chronoamperometry is a method of applying a constant potential to a working electrode to investigate the regular change of current with reaction time in an electrochemical reaction and the value of current (steady-state current) that can be maintained after a long-term chemical reaction. The smaller the current loss is, the larger the steady-state current value is, and the activity of the catalyst in the reaction process is correspondingly illustratedThe better the performance, the more stable. As can be understood from FIG. 4, 0.07mL of CeO₂Catalyst and no-supported CeO₂The electrochemical stability of the catalyst is better, and the fact that the catalyst is associated with CeO is proved₂The electrochemical stability also shows a tendency of increasing first and then decreasing. From the figure we also obtained that CeO was not added₂The stability of the catalyst in formic acid is better than that of other catalysts.

TABLE 1 supporting different CeO₂CO oxidation peak current potential and onset potential.

CO anti-poisoning test: at 0.5M H₂SO₄Activating the catalyst with the solution as electrolyte, introducing high-purity CO for 200 s after activation, and introducing N₂And removing the CO which is not adsorbed in the solution for 1.5 min. And performing CV scanning on the electrolyte, wherein the scanning speed is 50 mV/s, and the scanning range is-0.24-1.0V until the final two circles are overlapped. Table 1 shows the supported CeO read out from FIG. 5₂CO oxidation peak current potential and onset potential of the ternary alloy of (a). The addition of 0.07 mLCeO is seen by the initial potential value and the potential of the peak maximum current value₂There is a significant potential indicating the addition of 0.07 mLCeO₂Has very good catalysis effect on converting CO into CO₂Has good poisoning resistance. As can be seen from the data in Table 1, other contents of CeO₂Compared with the case of not adding CeO₂The anti-poisoning ability of the catalyst has a significant advantage, which shows that the anti-CO-poisoning ability of the catalyst can be improved after the catalyst is added.

Comparative example 1

On the basis of example 1, formaldehyde is not added, the characterization activity of the obtained catalyst is equivalent to the area specific activity and the mass specific activity of the unsupported Pt-Ni-Cu alloy catalyst to formic acid, and XRD (X-ray diffraction) characterization shows that the peak position of the Pt-Ni-Cu alloy is not shifted, which indicates that formaldehyde is used as CeO (CeO) in a reaction system₂An inducer loaded onto the surface of the alloy.

Claims (1)

1. Pt-Ni-Cu ternary alloy supported CeO for electrocatalysis₂The composite material and the preparation method thereof are characterized by comprising the following specific preparation steps:

(1) 1 mL of oleylamine corresponded to 3.44 mg of CeO₂Fully performing ultrasonic dispersion on the original solution, adding 0.05-0.3 mL of the original solution into a centrifuge tube, centrifuging, sucking supernatant liquid by using a liquid transfer gun until only sediment is left, and adding 0.7mL of ethanolamine for ultrasonic dispersion to uniformly disperse the supernatant liquid;

(2) 303.4 mg of glycine, 200 mg of polyvinylpyrrolidone (PVP) and 300 mg of sodium iodide are respectively weighed in a clean beaker;

(3) 2 mL of 20 mM H were added in sequence₂PtCl₆Aqueous solution, 1 mL of 20 mM CuCl₂Aqueous solution, 1 mL of 20 mM NiCl₂Adding the aqueous solution into the beaker of the sample in the step (2), and adding the fully dispersed CeO-containing solution₂Adding the ethanolamine into the beaker, stirring for 24 hours until the solution is blue and transparent, transferring 600 mu L (40%) of formaldehyde solution, slowly dropwise adding the formaldehyde solution into the beaker, and continuously stirring for 15 min;

(4) putting the fully stirred solution in the step (3) into a microwave reaction kettle, and preserving the heat for 30 min at 200 ℃;

(5) fully ultrasonically treating the solution in the kettle, transferring the solution into a centrifugal tube, centrifuging once at 10000 r/min for 15 min, pouring out the supernatant, adding water and ethanol into the centrifugal tube at a ratio of 1:1, ultrasonically treating the solution to ensure that the obtained precipitate is fully and uniformly dispersed, washing the precipitate for three times at 10000 r/min for 15 min, adding 1 mL of n-butylamine into the washed precipitate, ultrasonically treating the precipitate, and soaking the precipitate for one day;

(7) centrifuging the sample soaked with n-butylamine for one day at 10000 r/min for 15 min, pouring out the supernatant, adding water and ethanol 1:1 into a centrifugal tube, performing ultrasonic treatment, centrifuging at 10000 r/min for 15 min, washing for several times, and freeze-drying.

Images