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Thermodynamic assessment of an integrated biomass and coal co-gasification, cryogenic air separation unit with power generation cycles based on LNG vaporization

机译:基于LNG气化的具有发电循环的生物质和煤联合气化,低温空气分离装置的热力学评估

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摘要

A novel self-heat system which consists of a coal and biomass co-gasification process, low-temperature air separation based on the LNG vaporization, steam cycle, supercritical CO2 power generation unit and cryogenic carbon dioxide capture section is introduced and analyzed. Some new aspects of this study can be categorized as follows. There is no need to implement external heat sources and refrigeration units. Suitable process integration significantly decreases energy consumption and the heaters and coolers can be eliminated. Co-gasifier produces high yield synthesis gas to supply power and heat energy. The required pure oxygen (99.99%) for gasification is supplied from ASU. The specific energy required for high purity oxygen production is about 0.11 kW h/kg. The results show that the cold gas efficiency of gasifier is 81%. Also due to sufficient integration between LNG vaporization and other subsystems, 40459.53 kW energy is saved in the system. In cryogenic CO2 capture unit, 0.10 kW h/kg-CO2 is required to separate 99% carbon dioxide. Moreover, exergy and sensitivity analyses are carried out on the integrated process. Exergy efficiency and exergy destruction have been calculated for the main equipment of the system. The overall exergy destruction rate of the process is around 1.007 x 105 kW and heat exchangers have the highest portion of irreversibility. Finally, the effect of some significant parameters on the performance of the units is studied.
机译:介绍并分析了一种新型的自热系统,该系统由煤和生物质的共气化过程,基于液化天然气的气化的低温空气分离,蒸汽循环,超临界二氧化碳发电单元和低温二氧化碳捕集段组成。这项研究的一些新方面可以归纳如下。无需安装外部热源和制冷装置。适当的过程集成可以显着降低能耗,并且可以省去加热器和冷却器。辅助气化炉产生高产率的合成气以提供动力和热能。气化所需的纯氧(99.99%)由ASU提供。高纯度氧气生产所需的比能约为0.11 kW h / kg。结果表明,气化炉的冷气效率为81%。同样由于LNG蒸发和其他子系统之间的充分集成,系统中节省了40459.53 kW能量。在低温二氧化碳捕集单元中,分离99%的二氧化碳需要0.10 kW h / kg-CO2。此外,在综合过程中进行了火用和敏感性分析。已经计算出系统主要设备的火用效率和火用破坏。该过程的总火用破坏率约为1.007 x 105 kW,而热交换器具有最大的不可逆性。最后,研究了一些重要参数对单元性能的影响。

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