2022
DOI: 10.1021/acs.iecr.1c04476
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Impact of Kinetic Models on Methanol Synthesis Reactor Predictions: In Silico Assessment and Comparison with Industrial Data

Abstract: The reactor is one of the most important equipment to be designed for optimal process operations. An appropriate reactor modeling leads to an efficient and optimal process conceptual design, simulation, and eventually construction. The key for success in this step is mainly related to kinetics. The present work is centered toward process simulation and aims at comparing three different kinetic models for methanol synthesis. The comparison shows how the refitted Graaf model, presented in a previous study, effec… Show more

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Cited by 27 publications
(13 citation statements)
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“…Methanol synthesis is an exothermic reaction with a copper based catalyst which is sensitive to deactivation at relatively low temperature, so very good care is given to heat transfer. Kinetics in this section is modeled using the refitted Graaf model developed by Bisotti et al The reactor effluent is used to preheat the feed and then cooled with air to be finally condensed in a water-cooled exchanger. The crude methanol–water mixture is collected in a vessel, while the remaining syngas is sent to a compressor to recover pressure drops.…”
Section: Methodsmentioning
confidence: 99%
See 1 more Smart Citation
“…Methanol synthesis is an exothermic reaction with a copper based catalyst which is sensitive to deactivation at relatively low temperature, so very good care is given to heat transfer. Kinetics in this section is modeled using the refitted Graaf model developed by Bisotti et al The reactor effluent is used to preheat the feed and then cooled with air to be finally condensed in a water-cooled exchanger. The crude methanol–water mixture is collected in a vessel, while the remaining syngas is sent to a compressor to recover pressure drops.…”
Section: Methodsmentioning
confidence: 99%
“…It is primarily produced from methane and coal and considered a key molecule of the energy transition . CO 2 hydrogenation to methanol in particular is considered a promising pathway for carbon utilization …”
Section: Introductionmentioning
confidence: 99%
“…The pre-reforming unit is followed by a primary steam methane reformer (H101 in Figure ) operating at a pressure of 9 bar with a H 2 O/CH 4 ratio of 4. The unit implements the Xu-Froment kinetic model for its computations that was developed on Ni-Alumina Catalyst . The low pressure and high H 2 O/CH 4 ratio are chosen to achieve a methane conversion across the unit that is higher than 90%.…”
Section: Methodsmentioning
confidence: 99%
“…The unit implements the Xu-Froment 23 kinetic model for its computations that was developed on Ni-Alumina Catalyst. 24 The low pressure and high H 2 O/CH 4 ratio are chosen to achieve a methane conversion across the unit that is higher than 90%. This conversion is made more complex to achieve by the presence of hydrogen and carbon monoxide in the feed of the reformer.…”
Section: ■ Methodsmentioning
confidence: 99%
“…The difference lies in heat management, this led to a different strategy in the cooling operations. The unit was modelled as a HYSYS plug flow reactor with refitted Graaf's heterogeneous kinetic model, proposed in the work of Bisotti et al (2022) [4]. The hot products, rich in methanol and unconverted syngas, were cooled with (i) process-process heat exchanger, (ii) air cooler, and (iii) cooling water heat exchanger.…”
mentioning
confidence: 99%