Industrial Byproduct Hydrogen Recovery: Mixed Solvent Design, Process Optimization, and Assessment
Year: 2024
Type: article
Abstract: Recovering industrial byproduct hydrogen helps to minimize the environmental impact associated with hydrogen production. In this study, we propose an innovative approach for hydrogen recovery using an ionic liquid (IL)–methanol mixed solvent. By solving a computer-aided ionic liquid design-based mixed-integer nonlinear programming optimization problem, butylmethylammonium tetrafluoroborate ([N 4,1,0,0 ][BF 4 ]) is identified as the best cosolvent candidate. Subsequently, two process designs for hydrogen recovery using the [N 4,1,0,0 ][BF 4 ]-methanol mixed solvent are proposed and then rigorously simulated in Aspen Plus, followed by a comprehensive process assessment study. Results indicate that the absorption process making use of the IL–methanol mixed solvent is not competitive due to its demand for a large amount of solvent, leading to high energy consumption, carbon emissions, and total annual cost (TAC). Conversely, the IL–methanol-based extractive distillation process achieves notable energy savings of 26.0%, a 24.2% reduction in carbon emissions, and a 10.2% decrease in TAC compared to a benchmark hydrogen recovery process. This study underscores the flexibility and potential of the IL–methanol-based extractive distillation technology in industrial hydrogen recovery applications, paving the way for sustainable and efficient hydrogen production processes.
Source: Energy & Fuels
Authors: Ziqi Guo, Yang Lei, Yuming Chen, Yuming Chen, Xinyan Liu, Xiaoqin Wu, Yuqiu Chen, Yuqiu Chen
Language: English
Subfield: Control and Systems Engineering
Field: Engineering
Domain: Physical Sciences
Open Access status: green
Awards: 过程工业中尺度与宏尺度集成优化和参数耦联机制研究, G8535461776
OpenAlex ID: W4402265880
