Investigation of an intensified carbon capture process for onboard application

IF 4.2 3区 工程技术 Q3 ENERGY & FUELS
Seyedmohsen Hosseini, Renzo Di Felice
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引用次数: 0

Abstract

This study investigates an intensified carbon capture process designed to overcome the spatial constraints of shipboard applications. The objective is to minimize equipment size while maintaining performance, making carbon capture more practical for maritime use. A rotating packed bed (RPB) was evaluated as an alternative to conventional packed columns, using a 17 MW cargo ship as a case study. The RPB-based system was compared with a previously developed conventional design in terms of equipment dimensions and energy demand.
Process models were developed for the absorber and stripper units. The results showed that RPBs can significantly reduce the size of absorption columns while achieving comparable CO2 removal efficiency. Although absorbent regeneration was not significant, the enhanced heat transfer characteristics of the RPB suggested potential reductions in reboiler duty. A full RPB-based absorption–desorption cycle was also simulated, and the influence of key parameters on process performance was assessed. The results indicate that while the RPB can achieve a size reduction of more than threefold compared to a conventional packed column, this advantage entails approximately 25 % higher energy consumption, equivalent to 4.97 GJ per ton of captured CO2. The considerable size of a single RPB absorber also raises concerns regarding the mechanical feasibility of operating such a large rotor. Nevertheless, multi-stage configurations present a promising pathway for practical implementation. For example, a three-stage RPB can reduce the absorber’s outer diameter from 5.3 m to 3.1 m, with only a slight increase in energy demand to 5.19 GJ per ton of CO2.
一种用于车载应用的强化碳捕获工艺的研究
本研究探讨了一种强化碳捕获过程,旨在克服船舶应用的空间限制。目标是在保持性能的同时最小化设备尺寸,使碳捕获在海上应用中更加实用。以一艘17mw货船为例,对旋转填料床(RPB)作为传统填料柱的替代方案进行了评估。在设备尺寸和能源需求方面,将基于rpb的系统与之前开发的常规设计进行了比较。建立了吸收塔和汽提塔装置的工艺模型。结果表明,rpb可以显著减小吸收柱的尺寸,同时达到相当的CO2去除效率。虽然吸收剂再生不显著,但RPB增强的传热特性表明再锅炉负荷可能降低。模拟了基于rpb的全吸附-解吸循环,并评估了关键参数对工艺性能的影响。结果表明,与传统填料塔相比,RPB可以实现尺寸缩小三倍以上,但这一优势需要大约25%的能源消耗,相当于每吨捕获二氧化碳4.97 GJ。单个RPB吸收器的相当大的尺寸也引起了对操作这样一个大转子的机械可行性的关注。然而,多阶段配置为实际实施提供了一条有希望的途径。例如,三级RPB可以将吸收器的外径从5.3 m减少到3.1 m,而每吨二氧化碳的能源需求仅略微增加到5.19 GJ。
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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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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