合成气净化间接机制自热重整工艺与冷冻甲醇洗涤液的集成:以蓝氢为燃料的发电

IF 3.9 3区 工程技术 Q3 ENERGY & FUELS Chemical Engineering and Processing - Process Intensification Pub Date : 2025-02-25 DOI:10.1016/j.cep.2025.110248
Mohammadreza Malekli , Alireza Aslani , Tara Ghaffarinejad
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引用次数: 0

摘要

本文研究了总发电容量为420 MW的联合循环电厂天然气间接机理自热重整蓝色制氢装置的设计。排除燃烧前CO2捕集,以天然气联合循环电厂为参考案例进行建模。尽管采用传统配置,但汽提塔所需的所有热量都来自ATR工艺。此外,通过热集成将双压力有机朗肯循环与重整过程耦合起来。在recusol工艺中,以93.87%的CO2捕集率和~ 1.59 MJ/kg CO2的比加热消耗,可以产生约10.36 kg/s的H2,纯度为96.137 mol%,热值降低67.41 MJ/kg,冷气效率为78.42%。最终装置表明,总净发电量由353.24 MW提高到382.38 MW,净效率提高4.17%。此外,与没有有机朗肯循环的植物相比,能量损失显著减少了7.19%。最终,CO2比排放量从31.98 gCO2/kWh下降到29.55 gCO2/kWh, CO2年排放量从1231.66 kt /年显著下降到98.97 kt /年。
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Integration of indirect mechanism autothermal reforming process with chilled methanol scrubbing solution for syngas purification: Power generation exploiting blue hydrogen as fuel
This paper focuses on the design of blue hydrogen production through indirect mechanism autothermal reforming of natural gas applied to a combined cycle power plant with 420 MW total gross power generation. Excluding the pre-combustion CO2 capture, a natural gas combined cycle power plant has been modeled as a reference case. Despite the traditional configuration, all the required heat in stripping towers is generated from the ATR process. Moreover, a double-pressure organic Rankine cycle is coupled with the reforming process through heat integration. Approximately 10.36 kg/s H2 with 96.137 mol% purity, 67.41 MJ/kg Lower Heating Value, and 78.42% Cold Gas Efficiency is produced by 93.87% CO2 capture ratio in the Rectisol process with the specific heating consumption of ∼1.59 MJ/kg CO2. The final plant demonstrates that the total net power generation has improved from 353.24 MW to 382.38 MW, and net efficiency has been ameliorated by 4.17%. Additionally, the energy penalty is remarkably reduced by 7.19% compared to a plant without an organic Rankine cycle. Eventually, the specific CO2 emission decreased from 31.98 to 29.55 gCO2/kWh, as well as the annual emission of CO2 that has declined significantly from 1231.66 to 98.97 ktons/year.
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来源期刊
CiteScore
7.80
自引率
9.30%
发文量
408
审稿时长
49 days
期刊介绍: Chemical Engineering and Processing: Process Intensification is intended for practicing researchers in industry and academia, working in the field of Process Engineering and related to the subject of Process Intensification.Articles published in the Journal demonstrate how novel discoveries, developments and theories in the field of Process Engineering and in particular Process Intensification may be used for analysis and design of innovative equipment and processing methods with substantially improved sustainability, efficiency and environmental performance.
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