CC BY 4.0Nestler, FlorianFlorianNestlerFull, JohannesJohannesFullJäckle, Jan-MarcJan-MarcJäckleLinsenmeier, JohannesJohannesLinsenmeierRoob, JohannaJohannaRoobHadrich, Max J.Max J.HadrichSchaadt, AchimAchimSchaadt2022-09-152022-09-152022Note-ID: 000090CEhttps://publica.fraunhofer.de/handle/publica/425517https://doi.org/10.24406/h-42551710.1002/cite.20220002210.24406/h-4255172-s2.0-85129659248Utilization of the gas streams generated by the iron- and steel-making industry for the synthesis of synthetic fuels or chemicals is a promising way to kickstart a technical carbon cycle. Methanol synthesis from cleaned blast furnace gas is a challenge for process design and operation due to high inert gas contents and fluctuations in the gas supply. In this work, a miniplant setup with an adiabatic quench bed reactor was operated with cleaned blast furnace gas over a wide range of process conditions. The experimental data obtained were used to validate a simulation model of the miniplant setup with the perspective for an optimization of the process operational parameters. A high agreement between experimental and simulation data could be obtained, validating the applicability of the simulation approach presented in this work.enExperimental validationMethanol synthesisPower-to-LiquidReaction kineticsSteel mill gasesjournal article