Co2 Capture for the Silicon Process-Effects of Flue Gas Recirculation

V. Andersen, H. Knuutila, L. Braakhuis, Edin Myrhaug, K. Einarsrud, G. Tranell
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引用次数: 2

Abstract

Flue gas recirculation has been proposed as a potential process improvement for the silicon and ferrosilicon process. In this paper, flue gas flows and concentration from a 100 MW silicon production operation has been calculated for 0, 25, 50, 62.5 and 75 % flue gas recirculation. Using these flue gas flows as inputs in a carbon capture model shows that specific reboiler duty can be reduced from 3,55 GJ/mtCO2 to 2,85 GJ/mtCO2 by implementing 75 % flue gas recirculation. Cost estimation of the absorber, heat exchanger and blowers indicate a potential 13,3 M$ (62 %) cost reduction between 0 and 75 % FGR.
硅工艺的Co2捕集——烟气再循环效应
烟气再循环被认为是硅和硅铁工艺的潜在改进方法。本文对100 MW硅生产装置在烟气再循环率为0%、25%、50%、62.5%和75%时的烟气流量和浓度进行了计算。使用这些烟气流作为碳捕获模型的输入表明,通过实施75%的烟气再循环,可将再锅炉的特定负荷从3,55 GJ/mtCO2减少到2,85 GJ/mtCO2。对吸收器、热交换器和鼓风机的成本估算表明,在0 - 75%的FGR之间,潜在的成本降低了1330万美元(62%)。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
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