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IMPROVING PROCESS PERFORMANCES IN COAL GASIFICATION FOR POWER AND SYNFUEL PRODUCTION

机译:提高用于发电和合成的煤气化过程的性能

摘要

This paper is aimed at developing process alternatives of conventional coal gasification. A number of possibilities are presented, simulated and discussed, in order to improve the process performances, to avoid the use of pure oxygen, and to reduce the overall CO2 emissions. The different process configurations considered include both power production, by means of an Integrated Gasification Combined Cycle (IGCC) plant, and synfuel production, by means of Fischer-Tropsch (FT) synthesis. The basic idea is to thermally couple a gasifier, fed with coal and steam, to and a combustor where coal is burnt with air, thus overcoming the need of expensive pure oxygen as a feedstock. As a result no or little nitrogen is present in the syngas produced by the gasifier: the required heat is transferred by using an inert solid as the carrier, which is circulated between the two modules. First, a thermodynamic study of the dual bed gasification is carried out. Then a dual bed gasification process is simulated by Aspen PlusTM and the efficiency and overall CO2 emissions of the process are calculated and compared with a conventional gasification with oxygen. Eventually, the scheme with two reactors (gasifier-combustor) is coupled with an IGCC process. The simulation of this plant is compared with that of a conventional IGCC where the gasifier is fed by high purity oxygen. According to the configuration newly proposed the global plant efficiency increases by 27.9 % and the CO2 emissions decrease by 21.8 %, with respect to the performances of a conventional IGCC process.As a second possibility, the same gasifier-combustor scheme is coupled with a Coal To Liquid (CTL) process to convert the syngas into synthetic fuels by a FT reactor. It is shown that, if compared with a conventional CTL plant, the mass yield of liquid synthetic fuel is increased by 39.4 %, the CO2 emissions per unit of liquid fuel are decreased by 31.9 % and energy efficiency increases of by 71.1 %.
机译:本文旨在开发常规煤气化工艺的替代方案。提出,模拟和讨论了许多可能性,以改善工艺性能,避免使用纯氧并减少总的CO2排放量。所考虑的不同过程配置既包括通过整体气化联合循环(IGCC)装置进行的动力生产,也包括通过费托(FT)合成进行的合成燃料生产。基本思想是将装有煤和蒸汽的气化炉与燃烧室热耦合,在燃烧室中用空气燃烧煤,从而克服了昂贵的纯氧作为原料的需求。结果,在气化炉产生的合成气中几乎没有氮气存在:通过使用惰性固体作为载体来传递所需的热量,该惰性固体在两个模块之间循环。首先,进行了双床气化的热力学研究。然后通过Aspen PlusTM模拟双床气化过程,并计算该过程的效率和总CO2排放量,并将其与常规的氧气气化进行比较。最终,具有两个反应器(气化炉-燃烧器)的方案与IGCC工艺相结合。该工厂的模拟与传统IGCC的模拟进行了比较,在传统的IGCC中,气化炉由高纯度氧气供入。根据新提议的配置,相对于常规IGCC工艺的性能,全球工厂效率提高了27.9%,CO2排放降低了21.8%。作为第二种可能性,相同的气化炉-燃烧器方案与煤结合转液(CTL)工艺通过FT反应器将合成气转化为合成燃料。结果表明,与常规的CTL工厂相比,液态合成燃料的质量产率提高了39.4%,每单位液态燃料的CO2排放量降低了31.9%,能源效率提高了71.1%。

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