The Citing articles tool gives a list of articles citing the current article. The citing articles come from EDP Sciences database, as well as other publishers participating in CrossRef Cited-by Linking Program. You can set up your personal account to receive an email alert each time this article is cited by a new article (see the menu on the right-hand side of the abstract page).
Reactor configuration, operations and structural catalyst design in process intensification of catalytic reactors: A review
Gedefaw Asmare Tafete and Nigus Gabbiye Habtu Chemical Engineering and Processing - Process Intensification 184 109290 (2023) https://doi.org/10.1016/j.cep.2023.109290
Non-Idealities in Lab-Scale Kinetic Testing: A Theoretical Study of a Modular Temkin Reactor
Experimental methods in chemical engineering: High throughput catalyst testing — HTCT
Carlos Ortega, Daria Otyuskaya, Erik‐Jan Ras, Luis D. Virla, Gregory S. Patience and Hendrik Dathe The Canadian Journal of Chemical Engineering 99(6) 1288 (2021) https://doi.org/10.1002/cjce.24089
Accumulation and distribution of higher hydrocarbons in the pores of a cobalt catalyst during low-temperature Fischer–Tropsch fixed-bed synthesis
Reactor Selection for Upgrading Hemicelluloses: Conventional and Miniaturised Reactors for Hydrogenations
Stefan Haase, Cesar A. de Araujo Filho, Johan Wärnå, Dmitry Yu. Murzin and Tapio Salmi Processes 9(9) 1558 (2021) https://doi.org/10.3390/pr9091558
Hydrodynamics of Gas–Liquid Slug Flows in a Long In-Plane Spiral Shaped Milli-Reactor
Mei Mei, Francisco Felis, Gilles Hébrard, Nicolas Dietrich and Karine Loubière Theoretical Foundations of Chemical Engineering 54(1) 25 (2020) https://doi.org/10.1134/S0040579520010169
Novel continuous catalytic hydrogenation process for the synthesis of diacetone-d-allose
Anne Müller, Jana Kanz, Stefan Haase, Karin Becker and Hans-Matthias Vorbrodt Chemical Engineering and Processing: Process Intensification 113 2 (2017) https://doi.org/10.1016/j.cep.2016.10.013
Continuous Hydrogenation of L‐Arabinose and D‐Galactose in a Mini Packed‐Bed Reactor
Evaluation of reactor concepts for the continuous production of fine chemicals using the selective hydrogenation of cinnamaldehyde over palladium catalysts
Investigation of a packed bed in a mini channel with a low channel-to-particle diameter ratio: Flow regimes and mass transfer in gas–liquid operation
Robert Langsch, Johannes Zalucky, Stefan Haase and Ruediger Lange Chemical Engineering and Processing: Process Intensification 75 8 (2014) https://doi.org/10.1016/j.cep.2013.10.004
Impact of Spherical Catalyst Particles on Gas‐Liquid Flow Regimes in Minichannels with Square Cross Section