Simulation research on optimization of a 200 MW IGCC system

Ying Wang, Haoran Ning, Ying Sun
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Abstract

The integrated gasification combined cycle (IGCC) has increasingly attracted attention as a promising high-efficiency clean coal technology. The oxygen-to-carbon ratio (O/C), nitrogen reinjection coefficient (Xgn), and integration air separation coefficient (Xas) affect system performance greatly. Based on the selected coal type, this paper establishes a 200 MW IGCC system model with coal–water slurry gasification, matches the three-pressure reheating heat recovery steam generator and syngas coolers, simulates and calculates the system performance of O/C, Xas and Xgn using Thermo-flex software. From the perspective of the whole system, the optimal O/C of the system is obtained as 0.91 considering the syngas composition and gasification temperature. From the perspective of system efficiency, the Xgn is obtained as 60 % with the Xas of 20 %. The overall IGCC system model is optimized using the optimized O/C, Xgn, and Xas to obtain higher system power and efficiency, the system power generation efficiency can improve up to 51.52 %. A thermal balance diagram of the IGCC system is drawn using the calculation results and provides a reference for the future design and operation of IGCC systems.

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200mw IGCC系统优化仿真研究
综合气化联合循环作为一种极具发展前景的高效洁净煤技术日益受到人们的关注。氧碳比(O/C)、氮气回注系数(Xgn)和一体化空气分离系数(Xas)对系统性能影响较大。在选定煤种的基础上,建立了200 MW水煤浆气化IGCC系统模型,匹配了三压再加热余热蒸汽发生器和合成气冷却器,利用thermoflex软件对O/C、Xas和Xgn的系统性能进行了仿真计算。从整个系统来看,考虑合成气组成和气化温度,系统的最优O/C为0.91。从系统效率的角度来看,Xgn为60 %,Xas为20 %。采用优化后的O/C、Xgn和Xas对整个IGCC系统模型进行优化,获得更高的系统功率和效率,系统发电效率可提高51.52 %。根据计算结果绘制了IGCC系统的热平衡图,为今后IGCC系统的设计和运行提供参考。
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