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Direct formic acid fuel cell with vanadium sulfate oxide homogeneous assisted catalysis

A formic acid fuel cell and co-catalyst technology, which is applied to fuel cells, circuits, electrical components, etc., can solve the problem of reducing the loading of the main catalyst, and achieve the effect of avoiding the dehydration reaction of formic acid and avoiding CO poisoning.

Active Publication Date: 2019-12-13
ZHEJIANG UNIV
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

A hydroxyl group (OH) can be formed at the position of the Ru element, and the CO adsorbed on the platinum active site is oxidized to CO under the action of OH 2 and H 2 O, thereby eliminating the adsorption of CO and regaining the platinum active sites, however, reaction (5) is still the rate-determining step in the electrochemical oxidation of formic acid, and the enhanced reduction of platinum oxide is still the key factor to improve the performance of direct formic acid fuel cells
Moreover, on the surface of the limited carbon carrier, both the main catalyst and the co-catalyst must be loaded. Increasing the loading of the co-catalyst will inevitably lead to a decrease in the loading of the main catalyst, so the effects of the main catalyst and the co-catalyst cannot be maximized. Maximize

Method used

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  • Direct formic acid fuel cell with vanadium sulfate oxide homogeneous assisted catalysis
  • Direct formic acid fuel cell with vanadium sulfate oxide homogeneous assisted catalysis
  • Direct formic acid fuel cell with vanadium sulfate oxide homogeneous assisted catalysis

Examples

Experimental program
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Effect test

Embodiment 1

[0054] Example 1: Preparation of carbon-supported Pd catalyst

[0055] 10g glucose monohydrate and 10g urea (glucose to urea mass ratio 1:1) were dissolved in 20mL deionized water to obtain glucose urea solution; ) was dissolved in 443.4mL deionized water, then added to the glucose urea solution, and 10wt% hydrochloric acid was added dropwise to keep the pH value at a constant value; placed in a water bath at 85°C, and fully stirred. After 45 minutes of polymerization reaction, a commercially available carbon carrier XC-72 was added at a mass ratio of carbon carrier to palladium chloride of 90:10, stirred for 1 hour to form a suspension, and spray-dried to obtain a precursor. The precursor was placed in a tube furnace under N 2 Under the protection of the atmosphere, at 10°C min -1 Raise the temperature to 160°C for 2 hours at the same rate to fully polymerize the prepolymer, and then raise the temperature to 900°C for 2 hours at the same rate to complete the carbonization p...

Embodiment 2

[0056] Embodiment two: anion exchange resin treatment

[0057] Commercially available anion exchange resins are usually ion exchange resins containing chloride ions, Amberlite IRA402 was acid-boiled in 10wt% formic acid solution for 2 hours to realize ion exchange and obtain Amberlite containing formate ions IRA402, an anion exchange resin for direct formic acid fuel cell anode preparation obtained by washing with deionized water and drying: anion exchange resin treated with formic acid.

Embodiment 3

[0058] Embodiment three: anion exchange resin suspension preparation

[0059] 5g PBI is dissolved in 90g NMP, adds the formic acid treatment anion exchange resin that obtains in 5g embodiment two, in ZrO 2 Mill in a ball mill tank for 2 hours to obtain an anion exchange resin suspension.

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Abstract

The invention relates to a fuel cell technology and aims to provide a direct formic acid fuel cell with vanadium sulfate oxide homogeneous assisted catalysis. The preparation method for modified formic acid fuel in the fuel cell comprises the following steps of: heating one liter of concentrated sulfuric acid with a mass concentration of 98 wt% to 70-90 DEG C, adding 0.1-1 mol of NH4VO3 and conducting stirring and reacting for 5 h, after cooling to room temperature, adding 1-4 liters of formic acid aqueous solution with a mass concentration of 30-60 wt% to obtain modified formic acid fuel containing a (VO)SO4 cocatalyst. (VO)SO4 is added into the formic acid solution to play a co-catalytic role, dehydration reaction of formic acid on a solid catalyst is prevented, and catalyst poisoning iseffectively avoided. The cocatalyst exists in the formic acid solution, is not restricted by the supported area of the solid catalyst, can play the role of the cocatalyst to the maximum extent and does not reduce the supported amount of the main catalyst on the solid carrier. The active center is homogeneous and has high activity, and the electrochemical reaction speed of the formic acid is greatly improved. A new idea is provided for design and performance improvement of direct formic acid fuel cells.

Description

technical field [0001] The invention relates to fuel cell technology, in particular to a direct formic acid fuel cell with homogeneous assisted catalysis of vanadium oxide sulfate. Background technique [0002] A fuel cell is a high-efficiency energy conversion device that directly converts the chemical energy stored in the fuel into electrical energy. Because it does not need to go through the Carnot cycle, it has high energy density and energy conversion efficiency. It is a new type of green energy technology. In recent years, due to innovative breakthroughs in fuel cell (Fuel Cell) technology, coupled with multiple pressures such as environmental protection issues and energy shortages, governments of various countries and industries such as automobiles, electric power, and energy have gradually attached importance to the development of fuel cell technology. Fuel cell is a new power generation technology with high efficiency, low pollution and diversified energy sources. ...

Claims

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Application Information

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IPC IPC(8): H01M8/1009
CPCH01M8/1009Y02E60/50
Inventor 李洲鹏李艳刘宾虹
Owner ZHEJIANG UNIV
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