Disclosure of Invention
The invention aims to overcome the defects in the prior art and provide a self-supporting PtCo alloy nanoparticle catalyst with good catalytic activity, strong antitoxic ability and good mechanical property, and a preparation method and application thereof.
The purpose of the invention can be realized by the following technical scheme: a self-supporting PtCo alloy nanoparticle catalyst comprises three-dimensional porous nitrogen-doped carbon and Pt and Co coated inside the three-dimensional porous nitrogen-doped carbon, wherein the mass ratio of the Pt to the Co is (0.5-0.6): 1 the total mass of the Pt and the Co accounts for 43-48% of the mass of the catalyst, and the three-dimensional porous nitrogen-doped carbon is in an array structure. The invention adopts Pt and Co as the effective components of the catalyst, the combination of Pt and Co reduces the electron binding energy in Pt, and promotes C-H cracking reaction under low potential, thereby improving the activity and antitoxicity of the catalyst. Meanwhile, the precursor of the cobalt-based metal organic framework material is of a three-dimensional array structure, so that the porous nitrogen-doped carbon after calcination is also of an array structure. The highly graphitized porous nitrogen-doped carbon nanorod array has large specific surface area and high conductivity, provides ideal support for the dispersion of PtCO nano particles, and is favorable for promoting the migration of ions/protons; the doped nitrogen element can enhance the interaction between alloy particles and carbon and improve the stability of the catalyst; and the intrinsic catalytic capability of the porous nitrogen-doped carbon also makes a certain contribution to the improved catalytic activity.
A method for preparing the self-supporting PtCo alloy nanoparticle catalyst as described above, comprising the steps of:
(1) putting carbon cloth into an aqueous solution of acetone for ultrasonic treatment, washing and drying, and then putting the carbon cloth into a precursor solution to form a cobalt-based metal organic framework, wherein the precursor solution is a mixed aqueous solution of cobalt nitrate and dimethylimidazole;
(2) calcining the cobalt-based metal organic framework to obtain three-dimensional porous nitrogen-doped carbon coated with Co nanoparticles;
(3) soaking the obtained Co nanoparticle-coated three-dimensional porous nitrogen-doped carbon in H2PtCl4And (3) obtaining the self-supporting PtCo alloy nano-particle catalyst in a Pt solution.
The carbon cloth woven by the carbon fibers is a good three-dimensional conductive substrate material, so that the specific surface area of the prepared material can be increased, and the active sites can be increased; on the other hand, the active material grown on the carbon cloth can be directly used as a catalytic electrode, and the step of preparing the electrode like other powder catalysts is omitted. In the whole preparation process, Co is gradually replaced by Pt from outside to inside to form alloy particles.
The time for carrying out ultrasonic treatment on the carbon cloth in the aqueous solution of acetone is 20-30 min, and the carbon cloth is cleaned by ultrasonic.
Deionized water is adopted for washing, and the drying temperature is 60-80 ℃.
In the precursor solution, the molar ratio of cobalt nitrate to dimethyl imidazole is 1 (15-20).
The calcination is carried out on Ar and H2Wherein Ar is Ar and H290 to 95 percent of the total volume. H2The addition of the carbon nano-tube can promote the catalytic action of Co in the calcining process, and a plurality of carbon nano-tubes grow on the surface of the array structure, so that the specific surface area of the structure is increased.
Heating to 700-900 ℃ at a speed of less than 5 ℃/min, preserving heat for 2-4 h, and naturally cooling to room temperature. The cobalt-based metal organic framework array can be highly graphitized at 700-900 ℃, and the conductivity is increased.
Said H2PtCl4The concentration of the Pt solution is 0.5-2 mmol/L, and the Co nano-particle coated three-dimensional porous nitrogen-doped carbon is in H2PtCl4The soaking time in the Pt solution is 2-4 min.
Use of a self-supporting PtCo alloy nanoparticle catalyst as described above for use in the anode of a methanol fuel cell. The anode of the methanol fuel cell generates methanol oxidation reaction, and the cathode generates oxygen reduction reaction. The material prepared by the invention is a methanol oxidation catalyst, so the material is used for an anode of a methanol fuel cell.
Compared with the prior art, the beneficial effects of the invention are embodied in the following aspects:
(1) when the catalyst is used for the anode of a methanol fuel cell, the initial potential of methanol oxidation is high, and the current density of the anode is high;
(2) when the catalyst is used for an anode of a methanol fuel cell, the CO toxicity resistance and the durability are excellent.
Detailed Description
The following examples are given for the detailed implementation and specific operation of the present invention, but the scope of the present invention is not limited to the following examples.
Example 1
A preparation method of a self-supporting PtCo alloy nanoparticle catalyst comprises the following steps:
preparation of Co-MOFs nanorod array on carbon cloth
Firstly, selecting carbon cloth as a substrate, wherein the model is as follows: WOS 1002. And respectively putting the carbon cloth into acetone and deionized water for ultrasonic treatment for 20 minutes, finally washing with the deionized water, and putting into a forced air drying oven for drying.
Preparing a Co-MOFs precursor solution: 40ml of 25mM cobalt nitrate (Co (NO)3)2·6H2O) was added rapidly to 40ml of 0.4M dimethylimidazole (C)4H6N2) In an aqueous solution, and then stirred.
And soaking the treated carbon cloth in the Co-MOFs precursor solution at 30 ℃ for reaction for 4 hours. Then washing the product by deionized water.
And repeating the steps, and secondarily growing the Co-MOFs under the same temperature and reaction time.
Preparation of Co @ N-C nanorod array on carbon cloth
The Co-MOFs nanorod array prepared on the carbon cloth is subjected to Ar/H reaction at 800 DEG C2(5%H295% Ar) for 2 hours, wherein the heating rate is 5 ℃/min. Naturally cooling to obtain the Co @ N-C nanorod array structure (figure 1).
Preparation of PtCo @ N-C nanorod array on carbon cloth
The prepared PtCo @ N-C nanorod array on the carbon cloth was placed in a stirred 1mM chloroplatinic acid (H)2PtCl6·6H2O) for 3 minutes, labeled PtCo @ N-C. The reaction equation is:
Co+PtCl42-→Co2++Pt+4Cl-
the PtCo @ N-C nanorod array prepared on the carbon cloth is subjected to Ar/H reaction at 400 DEG C2(5%H295% Ar) for 1 hour, wherein the heating rate is 3.5 ℃/min. And naturally cooling to obtain the PtCo @ N-C nanorod array structure (shown in figure 2).
The mass of Pt and Co in the prepared PtCo @ N-C is 0.278mg cm-2And 0.533mg cm-2The corresponding atomic ratio is 14: 86.
The invention synthesizes a three-dimensional Co-MOFs nanorod structure with large specific surface area by a liquid phase method, obtains a Co @ N-C structure through annealing treatment, takes the Co @ N-C structure as a carrier, prepares a series of Pt loaded PtCo @ N-C catalysts by adopting a simple Pt precursor soaking method, and carries out system test and analysis on the electrocatalytic performance of the catalysts.
The electrocatalytic performance of the prepared PtCo @ N-C catalyst is tested by an electrochemical workstation under a three-electrode system. The PtCo @ N-C catalyst is used as a working electrode, Ag/AgCl (+0.197V vs RHE) soaked in a saturated KCl solution is used as a reference electrode, and a graphite rod is used as a counter electrode.
Before measurement, high-purity Ar is introduced into the electrolyte for 20 minutes,to remove CO and O in the solution2。
The electrochemical active area of the prepared PtCo @ N-C catalyst is 0.5M H2SO4In a solution of (a), wherein the test voltage is in the range of 0 to 1.0V vs RHE and the sweep rate is 50mV s-1。
The electrochemical active areas of the prepared PtCo @ N-C and Pt/C catalysts are respectively 20m2G and 14.2m2The/g, PtCo @ N-C catalyst exhibited a larger electrochemically active area (FIG. 3).
The methanol oxidation performance of the prepared PtCo @ N-C catalyst was improved by including 0.5M H2SO4And 0.5M CH3Obtained by testing a voltammetry Curve (CV) in an OH mixed solution, wherein the test voltage range is 0-1.2V vs. RHE, and the sweep rate is 50mV s-1。
The prepared PtCo @ N-C catalyst has more negative initial voltage (0.563V) than the Pt/C catalyst<0.642V) and greater positive peak current density (433.5mA mg-1>140mA mg-1). Thus, the PtCo @ N-C catalyst exhibited superior methanol oxidation activity (FIG. 4).
The methanol oxidation stability of the prepared PtCo @ N-C catalyst is 0.5M H2SO4And 0.5M CH3Obtained by testing a CV curve of 100 continuous cycles in an OH mixed solution, wherein the test voltage interval is 0-1.2V vs. RHE, and the sweep rate is 50mV s-1。
The anode peak current density retention of the prepared PtCo @ N-C and Pt/C catalysts after 100 cycles was 94.4% and 68.7% of the peak, respectively, indicating that the durability of the PtCo @ N-C catalysts was due to commercial Pt/C (FIG. 5).
The CO antitoxic performance of the prepared PtCo @ N-C catalyst is 0.5M H of CO saturation2SO4The test voltage interval is-0.1-1.4V vs RHE, and the sweep rate is 50mV s-1. High purity CO gas and A r gas were passed into the electrolyte for 15 minutes each before the measurement to ensure that the catalyst active sites were covered with sufficient CO and that the solution was free of CO.
The prepared PtCo @ N-C and Pt/C catalysts have CO desorption peaks at 0.92V and 1.03V respectively, and the more negative CO desorption peaks of PtCo @ N-C prove that the prepared PtCo @ N-C has more excellent CO CO-solubility (figure 6).
Thus, the PtCo @ N-C catalyst prepared in this example has excellent methanol oxidation current density, CO poisoning resistance, and durability.
Example 2
A similar preparation method to that of example 1 was employed, except that:
(1) the ultrasonic treatment time of the carbon cloth in the aqueous solution of acetone is 20min, and the drying temperature of the carbon cloth is 60 ℃;
(2) the molar ratio of cobalt nitrate to dimethyl imidazole in the precursor solution is 1: 15.
(3) calcining at Ar and H2Wherein Ar accounts for 90% of the total gas volume; the calcining temperature is 700 ℃, and the calcining time is 4 hours;
(4) h for soaking2PtCl4The concentration of the Pt solution is 0.5m mol/L, and the soaking time is 4 min.
The catalyst prepared in the embodiment is used for an anode of a methanol fuel cell, and tests show that the catalyst has higher current density and good CO anti-toxicity performance.
Example 3
A similar preparation method to that of example 1 was employed, except that:
(1) the ultrasonic treatment time of the carbon cloth in the aqueous solution of acetone is 30min, and the drying temperature of the carbon cloth is 80 ℃;
(2) the molar ratio of cobalt nitrate to dimethyl imidazole in the precursor solution is 1: 20.
(3) Calcining at Ar and H2Wherein Ar accounts for 90 to 95 percent of the total gas volume; the calcining temperature is 900 ℃, and the calcining time is 2 hours;
(4) h for soaking2PtCl4The concentration of the Pt solution is 2m mol/L, and the soaking time is 2 min.
The catalyst prepared in the embodiment is used for an anode of a methanol fuel cell, and tests show that the catalyst has higher current density and good CO anti-toxicity performance.