高效甲醇燃料电池技术研究进展

doi:10.19799/j.cnki.2095-4239.2025.0314

摘要/Abstract

摘要：

甲醇具有成本低、易储运、获取便捷等特点，“液态阳光”甲醇是我国能源结构绿色低碳发展的重要载体。基于甲醇的燃料电池在便携式电源、移动/固定式电站、车船动力等领域有广泛应用前景。本文介绍了各类甲醇燃料电池的类型与特点，从电效率角度分析了甲醇制氢与燃料电池的温度匹配、反应余热利用及发电效率的研究和应用进展。直接甲醇燃料电池功率密度较低、工作温度低、贵金属催化剂载量高，适用于便携式电源。甲醇重整制氢经纯化接氢燃料电池，因重整制氢难以充分利用氢燃料电池的副产热，系统综合电效率受限，但该技术路线成熟度高、小型化前景好，适用于各类电站。甲醇重整高温质子交换膜燃料电池电堆反应温度约200 ℃，改进传热结构可提高发电余热利用率，从而有望提升系统电效率，但仍需提高高温质子交换膜的寿命，降低催化剂用量。甲醇固体氧化物燃料电池的电堆反应温度高，余热可充分用于甲醇水溶液汽化和重整制氢，具有最高的理论电效率，研究重点在阳极抗积碳和改进高温热传导结构。最后本文总结各类甲醇燃料电池的热利用特点，提出了“定温度、调效率、强耦合”的燃料电池系统设计原则，以提高甲醇燃料电池的综合系统电效率。

关键词: 甲醇, 燃料电池, 能量效率, 温度, 热利用

Abstract:

Methanol, with its advantages of low cost, easy storage and transportation, and wide availability, serves as a critical carrier for China's green and low-carbon energy transition and is often referred to as "liquid sunlight." Methanol-based fuel cells have demonstrated broad application prospects in portable power systems, mobile/fixed power stations, and vehicle/ship propulsion. This paper introduces the types and characteristics of various methanol fuel cells and analyzes research and application progress in terms of electrical efficiency. The analysis focuses on temperature matching between methanol reforming and fuel cell operation, waste heat utilization, and power generation efficiency. Direct methanol fuel cells are characterized by low power density, low operating temperatures, and high noble metal catalyst loading, rendering them particularly well-suited for portable power applications. Despite its advanced technological status and considerable miniaturization potential, methanol reforming in conjunction with hydrogen fuel cells exhibits limited system efficiency, primarily due to the underutilization of waste heat from the fuel cell. High-temperature proton exchange membrane fuel cells (HT-PEMFCs), operating at approximately 200 ℃, have the potential to enhance waste heat recovery efficiency and, consequently, system efficiency through optimized thermal management. However, challenges persist in extending membrane lifespan and reducing catalyst usage. Methanol-fed solid oxide fuel cells, which operate at even higher temperatures, achieve the highest theoretical efficiency by fully utilizing waste heat for methanol/water vaporization and reforming. Current research focuses on carbon-resistant anodes and improved thermal conduction structures. In conclusion, the present document summarizes the thermal utilization characteristics of distinct methanol fuel cells and proposes a system design principle of "fixed temperature, adjustable efficiency, and strong thermal coupling" to maximize overall system efficiency.

Key words: methanol, fuel cell, energy efficiency, temperature, thermal recycling

中图分类号:

TK 91

谢峰, 孟海军, 雷宪章, 李新中, 丁飞, 邵志刚. 高效甲醇燃料电池技术研究进展[J]. 储能科学与技术, 2025, 14(11): 4237-4244.

Feng XIE, Haijun MENG, Xianzhang LEI, Xinzhong LI, Fei DING, Zhigang SHAO. Research Progress of High-Efficiency Methanol Fuel Cell Technology[J]. Energy Storage Science and Technology, 2025, 14(11): 4237-4244.

图/表 8

表1

图1

图2

表2

甲醇重整制氢反应类型及特点"

重整反应	反应式		反应温度	特点
甲醇水蒸气重整	CH₃OH+H₂O $⇌$ 3H₂+CO₂； H₂+CO₂ $⇌$ CO+H₂O	$∆ H$ =49.4 kJ/mol	约260 ℃或400 ℃	启动较慢，H₂含量高，需要外部供热
甲醇裂解制氢	CH₃OH $⇌$ 2H₂+CO	$∆ H$ =90.5 kJ/mol	约260 ℃	反应快，需要外部供热，易积碳、H₂含量低
部分氧化制氢	CH₃OH+1/2O₂ $⇌$ 2H₂+CO₂	$∆ H$ =-192.2 kJ/mol	约350 ℃	易启动、反应迅速，局部过热积碳、产物中H₂含量低
自热重整制氢	CH₃OH+(1-2a)H₂O+aO₂ $⇌$ CO₂+(3-2a)H₂	$∆ H$ =49.4-483.6a kJ/mol 0 $≤$ a $≤$ 0.5	约500 ℃^[18]	易启动、反应快；局部过热积碳、H₂含量低

表2

表3

图3

图4

图5

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名称	原理	电化学反应温度	综合电效率	特点	适用领域
直接甲醇燃料电池	通过电化学反应将甲醇水溶液的化学能转化为电能	室温~80 ℃	25%~35%	装置结构简单、比能量高、启动快；贵金属催化剂用量高、电流密度低	便携式电源
甲醇重整纯化质子交换膜燃料电池	甲醇经重整、纯化制备高纯氢气，通过质子交换膜燃料电池发电	室温~100 ℃	35%~45%	纯化技术多样，装置向小型化轻量化发展；发电余热难被制氢利用；	各类电站
甲醇重整高温质子交换膜燃料电池	甲醇重整气不经纯化进入高温质子交换膜燃料电池发电	160~200 ℃	35%~45%	产氢无需纯化，装置集成度较高，发电余热可部分被制氢利用	十千瓦级以内电站、增程器
甲醇固体氧化物燃料电池	甲醇在SOFC中内重整再发电	700-1000 ℃	30%~60%	启动慢、启停次数受限，发电余热易被重整利用	长时持续供电电源

技术路线	钯膜净化	变压吸附纯化	CO选择性氧化	CO选择性烷基化
工作温度	380~420 ℃	4~45 ℃	80~150 ℃	160~250 ℃
工作压力	1.5~2.0 MPa	0.1~4 MPa	常压	常压
启动时间	慢	快	较快	较快
催化剂	无	需要吸附剂，成熟	需要，成熟	需要，不成熟
引入杂质	无	吹扫气	O₂	无
产氢纯度	>99%	>99%	约70%	约75%
CO含量	<0.2 ppm	<0.2 ppm	约10 ppm	约10 ppm
纯化器体积(L/kW)	小	大(>500)	中(约45)	/