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A proton ceramic membrane fuel cell with composite structure and its preparation

A fuel cell and ceramic membrane technology, which is applied in fuel cells, circuits, electrical components, etc., can solve problems such as high cost, complicated operation, and increased grain boundary resistance, and is conducive to large-scale production and application, and low activation energy for transmission , the effect of reducing the interface resistance

Active Publication Date: 2021-07-20
DALIAN INST OF CHEM PHYSICS CHINESE ACAD OF SCI
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

At present, proton ceramic membrane fuel cells are mainly based on doped BaCeO 3 Base, BaZrO 3 The base is an electrolyte, which has high intrinsic proton conductivity, but poor sintering activity. For example, the sintering temperature of pure BZY is usually between 1700°C and 2200°C. Excessively high sintering temperature not only wastes energy, but also causes serious Ba volatilization, which affects the electrolyte. The actual ionic conductivity of
In addition, most of the proton ceramic membrane electrolytes are alkaline oxides, which have the problem of poor stability in acidic atmosphere.
Common methods for preparing proton ceramic membranes at low temperature: on the one hand, adding additives and using liquid phase sintering to promote electrolyte densification, but this method tends to leave impurity phases in the grain boundaries, which increases the grain boundary resistance and reduces battery performance; on the other hand, pulsed laser deposition , magnetron sputtering, chemical vapor deposition and other methods have been applied to prepare proton ceramic membranes, but the operation is complicated and the cost is high, which is not conducive to mass production

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0013] The cathode, electrolyte and anode slurries were prepared according to the casting slurry formula, and the three-layer stacked BSCF / BZY / BZY-NiO obtained by casting was co-fired at 1200°C for 8 hours, and the densities were 96.3% and 92.0%, respectively. The cathode dense layer and the anode dense layer are 2 microns. The pre-prepared cathode and anode screen printing pastes were coated on the surface of the dense layer, dried at room temperature for 8 hours, and sintered at 700°C for 2 hours. The thickness of the cathode porous layer and the anode porous layer was 600 microns, and the thickness of the electrolyte porous layer was The thickness is 15 microns, and a five-layer stacked BSCF / BSCF / BZY / BZY / BZY-NiO / BZY-NiO composite structure proton ceramic membrane fuel cell is obtained. The working conditions for testing battery performance are: containing high-purity H 2 As fuel gas, the flow rate is 10mL / min; air is the oxidant, the flow rate is 10mL / min, the open circuit...

Embodiment 2

[0015] The cathode, electrolyte and anode slurries were prepared respectively according to the casting slurry formula, and the three-layer stacked BZY / BCZY / BCZY-NiO obtained by casting was co-fired at 1150°C for 8 hours, and the densities were 97.1% and 90.0%, respectively. The cathode dense layer and the anode dense layer are 3 microns. The pre-prepared cathode and anode screen printing pastes were coated on the surface of the dense layer, dried at room temperature for 5 hours, and sintered at 800°C for 5 hours. The thickness of the cathode porous layer and the anode porous layer was 650 microns, and the thickness of the electrolyte porous layer was The thickness is 10 microns, and a proton ceramic membrane fuel cell with LSCF / LSCF / BZY / BCZY / BCZY-NiO / BCZY-NiO composite structure is obtained. The working conditions for testing battery performance are: containing high-purity H 2 As fuel gas, the flow rate is 10mL / min; air is the oxidant, the flow rate is 10mL / min, the open circ...

Embodiment 3

[0017] The cathode, electrolyte and anode slurries were prepared respectively according to the casting slurry formula, and the three-layer stacked BSC / BCZYYb / BZY-NiO obtained by casting was co-fired at 1250°C for 4 hours, and the densities were 96.3% and 92.0%, respectively. The cathode dense layer and the anode dense layer are 4 microns. The pre-prepared cathode and anode screen printing pastes were coated on the surface of the dense layer, dried at room temperature for 3 hours, and sintered at 750°C for 2 hours. The thickness of the cathode porous layer and the anode porous layer were 800 microns, and the thickness of the electrolyte porous layer was A proton ceramic membrane fuel cell with a five-layer stacked BSC / BSC / BCZYYb / BZY-NiO / BZY-NiO composite structure is obtained. The working conditions for testing battery performance are: containing high-purity H 2 As fuel gas, the flow rate is 8mL / min; air is the oxidant, the flow rate is 8mL / min, the open circuit voltage at 500...

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Abstract

The invention relates to a proton ceramic membrane fuel cell with composite structure. The fuel cell is composed of five parts: a cathode porous layer, an electrolyte porous layer, an anode porous layer, a cathode dense layer and an anode dense layer. Among them, the cathode porous layer and the anode porous layer play the role of gas transport and surface catalysis; the cathode dense layer and the anode dense layer play the role of blocking gas and improving interface connection; the electrolyte porous layer plays the role of conducting ions and blocking electrons. The proton ceramic membrane fuel cell with composite structure can reduce the preparation temperature to 1200°C-1300°C, breaking through the problems of traditional proton-type electrolytes such as high-temperature difficulty in sintering and high interface resistance, thereby reducing the preparation cost and expanding its application range.

Description

technical field [0001] The invention belongs to the field of solid oxide fuel cells, in particular to a proton ceramic membrane fuel cell with a composite structure. Background technique [0002] Traditional solid oxide fuel cells use oxygen ions as carriers, and have problems such as difficult sealing, long start-up and stop times, and serious diffusion reactions of various components at high operating temperatures (800°C-1000°C). Solid oxide fuel cells use protons as carriers. The theoretical transport activation energy of protons is three orders of magnitude lower than that of oxygen ions, and the operating temperature can be reduced to between 350°C and 550°C. potential. At present, proton ceramic membrane fuel cells are mainly based on doped BaCeO 3 Base, BaZrO 3 The base is an electrolyte, which has high intrinsic proton conductivity, but poor sintering activity. For example, the sintering temperature of pure BZY is usually between 1700°C and 2200°C. Excessively hig...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): H01M8/1231H01M8/1213H01M8/1253H01M8/126
CPCH01M8/1213H01M8/1253H01M8/126H01M2008/1293H01M8/1231Y02E60/50
Inventor 程谟杰戚惠颖赵哲
Owner DALIAN INST OF CHEM PHYSICS CHINESE ACAD OF SCI
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