Design of a Renewable Methanol Production Process from Biogas: Analysis of the Influence of the Operating Pressure in the Synthesis Loop

IF 3.8 3区 工程技术 Q2 ENGINEERING, CHEMICAL
M. Victoria Del Pópolo Grzona, Eduardo M. Izurieta, Eduardo López, Marisa N. Pedernera
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Abstract

This study presents the design and analysis of an energy-integrated process for producing green methanol from biogas. Emphasizing the need for sustainable fuel solutions, the paper explores the use of biogas, purified to biomethane, as a feedstock for methanol synthesis. The process involves a convective reformer with bayonet-type tubes for syngas production and a multitubular methanol synthesis reactor. The integration of thermal energy is a core feature, ensuring the process is self-sufficient. Key aspects analyzed include the impact of methanol synthesis loop pressure (30–90 bar) on performance metrics such as carbon and energy efficiency and CAPEX/OPEX of the loop. An optimum operating pressure of 40 bar was found. Simulation results indicate high methane conversion in the reformer (87.34%) and effective internal heat recovery due to the bayonet-type tubes (19%). The overall process achieves a carbon efficiency of 48.5% and an energy efficiency of around 64%.

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来源期刊
Industrial & Engineering Chemistry Research
Industrial & Engineering Chemistry Research 工程技术-工程:化工
CiteScore
7.40
自引率
7.10%
发文量
1467
审稿时长
2.8 months
期刊介绍: ndustrial & Engineering Chemistry, with variations in title and format, has been published since 1909 by the American Chemical Society. Industrial & Engineering Chemistry Research is a weekly publication that reports industrial and academic research in the broad fields of applied chemistry and chemical engineering with special focus on fundamentals, processes, and products.
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