嚴建華、杜長明著的《等離子體重整乙醇制氫
技術(英文版)(精)》對采用等離子體或等離子體—
催化工藝重整諸如乙醇等可再生原料制氫的研究進
行了介紹。利用新型等離子體工藝及等離子體催化
聯合工藝可減少氮氧化物排放，且能量循環中減少
“碳跡”，因而在再生資源制氫領域上表現出了強
大的潛力。實驗結果表明將等離子體與催化工藝相
結合可產生協同作用。由於具有良好的重整能力及
產氫效率，該技術將可望掀起新一輪重整工藝風暴
，並吸引眾多研究者進行綠色能源制取工藝的研究
。本書介紹了輸入功率、反應器結構、反應溫度、
載氣類型及原料組分等影響因素對重整效率的影響
。為進一步了解和評估重整效率，本書還對乙醇重
整的多種模型進行介紹，比較了不同等離子體反應
器重整乙醇的效果，並從各等離子體類型的特征對
其進行具體分析。本書在最後展望了未來該領域可
能的研究發展方向，並預測了新一代燃料制氫工藝
的發展及趨勢。

1 Plasma for Ethanol Reforming
1.1 Hydrogen and Plasma
1.2 Reforming Technologies of Liquid Fuel
1.2.1 CO2 Reforming
1.2.2 Partial Oxidation Reforming
1.2.3 Steam Reforming
1.2.4 Autothermal Reforming
1.2.5 Comparison Among Different Reforming Processes
1.3 Hydrogen Production by Ethanol Reforming
1.3.1 Catalytic Ethanol Reforming for Hydrogen Production
1.3.2 Plasma Ethanol Reforming for Hydrogen Production
References
Non-thermal Are Plasma for Ethanol Reforming
and Hydrogen Production
2.1 Non-thermal Plasma
2.2 Non-thermal Arc Plasma Reforming of Ethanol to Produce
Hydrogen
2.3 Factors Affecting on Plasma Reforming of Ethanol
2.3.1 Effects of the Components of the Materials
2.3.2 Effects of the Carrier Gas
2.3.3 Effects of the Input Power
2.3.4 Effects of Other Factors
2.4 Comparison of the Non-thermal Plasma Reforming of Ethanol
2.5 Developmental Trends of the Non-thermal Arc Plasma
Reforming of Ethanol
References
3 Hydrogen from Ethanol by a Plasma Reforming System
3.1 Introduction
3.2 Materials and Methods
3.2.1 Experimental Setup
3.2.2 Calculation
3.3 Results and Discussion
3.3.1 Effect of the O/C Ratio
3.3.2 Effect of the S/C Ratio
3.3.3 Effect of the Input Power
3.3.4 Effect of the Ethanol Flow Rate
3.4 Conclusion
References
4 Hydrogen from Ethanol by a Miniaturized Plasma
Reforming System
4.1 Introduction
4.2 Experimental Setup
4.3 Results and Discussion
4.3.1 Voltage-Current Characteristic
4.3.2 Effect of the O/C Ratio
4.3.3 Effect of the S/C Ratio
4.3.4 Effect of the Ethanol Flow Rate
4.4 Conclusion
References
Plasma-Catalytic Reforming for Hydrogen Generation