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首页> 外文期刊>Energy Technology: Generation,Conversion,Storage,Distribution >Performance Analysis of a New Integrated Gasification Technology Driven by Biomass for Hydrogen and Electricity Cogeneration with a Dual Chemical Looping Process
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Performance Analysis of a New Integrated Gasification Technology Driven by Biomass for Hydrogen and Electricity Cogeneration with a Dual Chemical Looping Process

机译:生物质驱动的氢气和电力热电联产双化学循环新综合气化技术的性能分析

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摘要

A process based on biomass gasification integrated with a dual chemical looping technology, namely, chemical looping air separation and iron-based chemical looping combustion, is proposed to investigate the performance of hydrogen and electricity cogeneration from a thermodynamic perspective. The effects of four vital ratios, namely, steam to biomass, oxygen to biomass, Fe2O3 to carbon, and flue gas to Mn2O3, on the thermodynamic performances of this process are investigated. Meanwhile, a T-Q diagram is involved in the validation of the feasibility of heat-exchange networks in this process. In parallel, the system efficiencies (such as total energy efficiency and exergy efficiency) are evaluated. The exergy destruction of this process is also analyzed. As a result, the total energy and exergy efficiencies are calculated to be 66.23 and 58.10%, respectively. Most exergy destruction is caused by the gasifier, which accounts for 40.90% of the total exergy destruction.
机译:提出了一种基于生物质气化并结合双重化学循环技术的工艺,即化学循环空气分离和铁基化学循环燃烧,从热力学角度研究了氢和电热电联产的性能。研究了蒸汽与生物质,氧气与生物质,Fe2O3与碳以及烟道气与Mn2O3四种重要比对该工艺的热力学性能的影响。同时,在此过程中,T-Q图参与了热交换网络可行性的验证。同时,评估系统效率(例如总能效和火用效率)。还分析了该过程的火用破坏。结果,总能量效率和火用效率分别为66.23%和58.10%。大部分的火用破坏是由气化炉造成的,占总火用破坏的40.90%。

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