An efficient low-carbon hydrogen production system based on novel staged gasification coupling with chemical looping technology

IF 10.9 1区 工程技术 Q1 ENERGY & FUELS Energy Conversion and Management Pub Date : 2025-02-13 DOI:10.1016/j.enconman.2025.119625
Shengping Zhang , Liangguo Lv , Luxuan Liu , Fei Dai , Jun Sui
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Abstract

Efficient hydrogen production and decarbonization through coal gasification still suffers from significant challenges. In this work, a novel and efficient low-carbon hydrogen production method via coal staged gasification coupling chemical looping technology was innovatively proposed, the method exhibits potential advantages in improving hydrogen production efficiency and achieving near-zero energy CO2 capture. Moreover, the chemical recuperation method that efficiently recovers the exhaust heat of the system is also employed to further enhance the gasification efficiency. Thermodynamic analysis results indicate that the cold gas efficiency of staged coal gasification, composed of coal pyrolysis and coke-CO2 gasification, reaches 85.04 %. By coupling chemical looping technology using FeO/Fe3O4 as an oxygen carrier, the corresponding hydrogen production efficiency achieves 65.32 %, with CO2 enrichment concentration reaching 92.14 %, thereby enabling zero-energy CO2 capture. Additionally, thermodynamic exergy balance analysis shows that the exergy efficiency of the new method for hydrogen production reaches approximately 64.51 %. The staged gasification, chemical looping, and heat exchange processes are identified as key contributors to exergy destruction. The energy utilization diagram methodology is used to further elucidate the mechanism of exergy destruction from the perspective of the level difference between the energy donor and the energy acceptor. Moreover, the new method is also compared with conventional coal-to-hydrogen gasification technology. This work can serve as significant guidance for the development of novel low-carbon coal gasification hydrogen production technologies.

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基于新型分段气化耦合化学循环技术的高效低碳制氢系统
通过煤气化高效制氢和脱碳仍然面临重大挑战。本文创新性地提出了一种新型高效的煤级气化耦合化学环技术低碳制氢方法,该方法在提高制氢效率和实现近零能耗CO2捕集方面具有潜在优势。此外,还采用了有效回收系统余热的化学回收方法,进一步提高了气化效率。热力分析结果表明,由煤热解和焦炭- co2气化组成的煤气化阶段冷气效率达到85.04%。通过以FeO/Fe3O4为氧载体的耦合化学环技术,相应的制氢效率达到65.32%,CO2富集浓度达到92.14%,从而实现零能量CO2捕集。此外,热力学用能平衡分析表明,新制氢方法的用能效率约为64.51%。阶段气化、化学循环和热交换过程被认为是造成火用破坏的关键因素。利用能量利用图方法,从能量供体和能量受体的能级差异角度进一步阐明了能量破坏的机理。并与传统的煤制氢技术进行了比较。这项工作对新型低碳煤气化制氢技术的发展具有重要的指导意义。
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来源期刊
Energy Conversion and Management
Energy Conversion and Management 工程技术-力学
CiteScore
19.00
自引率
11.50%
发文量
1304
审稿时长
17 days
期刊介绍: The journal Energy Conversion and Management provides a forum for publishing original contributions and comprehensive technical review articles of interdisciplinary and original research on all important energy topics. The topics considered include energy generation, utilization, conversion, storage, transmission, conservation, management and sustainability. These topics typically involve various types of energy such as mechanical, thermal, nuclear, chemical, electromagnetic, magnetic and electric. These energy types cover all known energy resources, including renewable resources (e.g., solar, bio, hydro, wind, geothermal and ocean energy), fossil fuels and nuclear resources.
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