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Feasibility Analysis of Syngas Production via CO2 Absorption Enhanced Gasifier for Ammonia Synthesis

机译:通过CO2吸收增强气化炉生产氨气合成气的可行性分析

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摘要

An alternative process of syngas production for ammonia synthesis was proposed in this paper.Syngas is made of coal and coal mine gas(CMM)by CO2 absorption enhanced gasification.Due to higher N2 content in CMM,it is possible to remove N2 supplement section or to replace air gasification by steam gasification.With the in-situ absorption of CO2,the syngas compositions at gasifier outlet can meet the inlet contents criteria of syngas refinery section which should be φ(H2)/φ(N2)= 3 and φ(CO2+CO)< 0.30%.In order to analyze the feasibility and operation conditions of the proposed process,syngas production reactor was simulated by thermodynamic model,from which the variations of syngas compositions with operation parameters were studied.Based on this work,it is able to determine the suitable operation parameters for gasifier operation and corresponding CMM flow rate.Considering the explosion limits variation of pressurized CMM,the feasible parameters for O2 removal reactor operation was calculated.Analysis results indicate that it is feasible to produce syngas for NH3 synthesis by coal and CMM co-gasification with in-situ CO2 capture.Meanwhile,it is advantage to simplify components adjustment section and syngas purification section.
机译:本文提出了一种合成氨气的合成气生产方法。合成气由煤和煤矿瓦斯(CMM)通过CO2吸收增强的气化制得。由于CMM中N2含量较高,因此可以去除N2补充段或通过原位吸收CO2,气化炉出口的合成气成分可以满足合成气精炼段入口含量标准,即φ(H2)/φ(N2)= 3和φ( (CO2 + CO)<0.30%。为分析提出的方法的可行性和操作条件,利用热力学模型对合成气生产反应器进行了模拟,研究了合成气组成随操作参数的变化。能够确定适合气化炉运行的运行参数和相应的三坐标测量机流量。考虑到加压三坐标测量机的爆炸极限变化,计算了脱氧反应器运行的可行参数。分析结果表明,将煤与三坐标测量机共气化并原位捕集CO 2制取NH 3合成气是可行的。同时,简化了组分调节段和合成气净化段是有利的。

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