Transforming CO2 into Synthetic Fuels: Modeling, Simulation, and Optimization Analysis of Methanol Production from Industrial Wastes

被引:4
作者
Kontou, Vasiliki [1 ]
Peppas, Antonis [2 ]
Kottaridis, Sotiris [2 ]
Politi, Chrysa [2 ]
Karellas, Sotirios [1 ]
机构
[1] Natl Tech Univ Athens, Sch Mech Engn, Sect Thermal Engn, Lab Thermal Proc, 9 Heroon Polytech St, Zografos 15780, Greece
[2] Natl Tech Univ Athens NTUA, Sch Min & Met Engn, Athens 15780, Greece
来源
ENG | 2024年 / 5卷 / 03期
关键词
decarbonization; carbon capture and utilization; CO2; hydrogenation; methanol; hydrogen; thermodynamic analysis; optimization; Aspen Plus; containerized; portable; PRODUCTION PLANT; HYDROGENATION;
D O I
10.3390/eng5030070
中图分类号
T [工业技术];
学科分类号
08 ;
摘要
Carbon capture and utilization (CCU) has emerged in recent years as a promising decarbonization solution for hard-to-abate industries. Compared to carbon capture and storage (CCS), CCU aims not for the storage of carbon dioxide (CO2) but for its use in the production of synthetic fuels, such as synthetic methanol (MeOH). Synthetic MeOH is produced through CO2 hydrogenation, utilizing green hydrogen (H-2). Efficient use of CO2 and H-2 feedstocks is essential to maximize the carbon reduction potential and energy efficiency of the process. This study performed an optimization analysis on a small-scale, containerized, and portable CO2 hydrogenation unit with a 5 kg MeOH/h production capacity goal, focusing on carbon conversion efficiency (CCE), MeOH yield, H-2 consumption, and MeOH purity. The analysis was conducted using Aspen Plus V12. A single-pass model was used first to evaluate an initial reactor design. The reactor was then re-designed according to the results of the gas hourly space velocity (GHSV). The model was then expanded to include a recycling loop and the final reactor design was validated, aiming to maximize overall efficiency. The effects of the operational parameters including the reactor inlet temperature, reactor pressure, thermal fluid temperature, and condensation temperature were examined. The model was then further expanded to include the MeOH distillation process, and the effect of the distillation temperature was examined. The final product of the analysis was a fully-defined and optimized unit, achieving an 87.97% CCE and an 84.99% MeOH yield, consuming 1.11 kg H-2/h for the production of 5.01 kg MeOH/h of 99.86 wt% purity. This study can provide valuable information and guidelines for designing small-scale, containerized, and portable CO2 hydrogenation units, which can serve as alternative solutions to address issues of H-2 production and transportation related to large-scale installations.
引用
收藏
页码:1337 / 1359
页数:23
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