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Hydrogen generation from ethanol using plasma reforming technology(等離子體重整乙醇制氫技術(shù))

Hydrogen generation from ethanol using plasma reforming technology(等離子體重整乙醇制氫技術(shù))

定 價(jià):¥98.00

作 者: 嚴(yán)建華 著
出版社: 浙江大學(xué)出版社
叢編項(xiàng):
標(biāo) 簽: 暫缺

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ISBN: 9787308187664 出版時(shí)間: 2019-02-01 包裝: 平裝-膠訂
開本: 16開 頁(yè)數(shù): 字?jǐn)?shù):  

內(nèi)容簡(jiǎn)介

  嚴(yán)建華、杜長(zhǎng)明著的《等離子體重整乙醇制氫技術(shù)(英文版)(精)》對(duì)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(jìn)行了介紹。利用新型等離子體工藝及等離子體催化聯(lián)合工藝可減少氮氧化物排放,且能量循環(huán)中減少“碳跡”,因而在再生資源制氫領(lǐng)域上表現(xiàn)出了強(qiáng)大的潛力。實(shí)驗(yàn)結(jié)果表明將等離子體與催化工藝相結(jié)合可產(chǎn)生協(xié)同作用。由于具有良好的重整能力及產(chǎn)氫效率,該技術(shù)將可望掀起新一輪重整工藝風(fēng)暴,并吸引眾多研究者進(jìn)行綠色能源制取工藝的研究。本書介紹了輸入功率、反應(yīng)器結(jié)構(gòu)、反應(yīng)溫度、載氣類型及原料組分等影響因素對(duì)重整效率的影響。為進(jìn)一步了解和評(píng)估重整效率,本書還對(duì)乙醇重整的多種模型進(jìn)行介紹,比較了不同等離子體反應(yīng)器重整乙醇的效果,并從各等離子體類型的特征對(duì)其進(jìn)行具體分析。本書在后展望了未來(lái)該領(lǐng)域可能的研究發(fā)展方向,并預(yù)測(cè)了新一代燃料制氫工藝的發(fā)展及趨勢(shì)。

作者簡(jiǎn)介

暫缺《Hydrogen generation from ethanol using plasma reforming technology(等離子體重整乙醇制氫技術(shù))》作者簡(jiǎn)介

圖書目錄

1 Plasma for Ethanol Reforming n
1.1 Hydrogeand Plasma n
1.2 Reforming Technologies of Liquid Fuel n
1.2.1 CO2 Reforming n
1.2.2 Partial OxidatioReforming n
1.2.3 Steam Reforming n
1.2.4 Autothermal Reforming n
1.2.5 ComparisoAmong Different Reforming Processes n
1.3 HydrogeProductioby Ethanol Reforming n
1.3.1 Catalytic Ethanol Reforming for HydrogeProduction
1.3.2 Plasma Ethanol Reforming for HydrogeProduction
References n
Non-thermal Are Plasma for Ethanol Reforming n
and HydrogeProduction
2.1 Non-thermal Plasma n
2.2 Non-thermal Arc Plasma Reforming of Ethanol to Produce n
Hydrogen
2.3 Factors Affecting oPlasma Reforming of Ethanol n
2.3.1 Effects of the Components of the Materials n
2.3.2 Effects of the Carrier Gas n
2.3.3 Effects of the Input Power n
2.3.4 Effects of Other Factors n
2.4 Comparisoof the Non-thermal Plasma Reforming of Ethanol n
2.5 Developmental Trends of the Non-thermal Arc Plasma n
Reforming of Ethanol n
References n
3 Hydrogefrom Ethanol by a Plasma Reforming System n
3.1 Introduction
3.2 Materials and Methods n
3.2.1 Experimental Setup n
3.2.2 Calculation
3.3 Results and Discussion
3.3.1 Effect of the O/C Ratio n
3.3.2 Effect of the S/C Ratio n
3.3.3 Effect of the Input Power n
3.3.4 Effect of the Ethanol Flow Rate n
3.4 Conclusion
References n
4 Hydrogefrom Ethanol by a Miniaturized Plasma n
Reforming System n
4.1 Introduction
4.2 Experimental Setup n
4.3 Results and Discussion
4.3.1 Voltage-Current Characteristic n
4.3.2 Effect of the O/C Ratio n
4.3.3 Effect of the S/C Ratio n
4.3.4 Effect of the Ethanol Flow Rate n
4.4 Conclusion
References n
Plasma-Catalytic Reforming for HydrogeGeneration
from Ethanol n
5.1 Introduction
5.2 Experimental Setup n
5.2.1 Plasma-Catalytic Setup n
5.2.2 Catalysts Characterization
5.3 Results and Discussion
5.3.1 Effect of the O/C Ratio n
5.3.2 Effect of the S/C Ratio n
5.4 Conclusion
References n
6 Mechanism for the Plasma Reforming of Ethanol n
6.1 Mechanism Analysis of the Single Plasma Reforming of Ethanol n
6.1.1 Electron-Molecule Collision
6.1.2 Free Radical Reaction
6.1.3 The Generatioand Conversioof the MaiProducts n
6.1.4 Suppressioand Removal of CarboDeposition
ithe Reforming Process n
6.1.5 Removal of NOr ithe Process of Reforming n
6.2 Mechanism Analysis of the Plasma-Catalytic Reforming n
of Ethanol n
6.2.1 Related Mechanism of the Catalytic Reforming n
of Ethanol n
6.2.2 Effects of Plasma othe Surface Characteristics n
of the Catalyst n
6.2.3 The Surface Reactioof the Electronic/Radical-Catalyst n
6.3 ComparisoBetweePlasma Reforming and n
Plasma-Catalyst Reforming n
6.4 Summary n
References n
7 Outlook n
Index 

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