Kuhlmann, HannsHannsKuhlmannMöller, MarcelMarcelMöllerSkiborowski, MirkoMirkoSkiborowski2020-12-042020-12-042019-03Chemie-Ingenieur-Technik 3 (91): 336-348 (2019-03)http://hdl.handle.net/11420/8138The current article presents the extension of a recently developed optimization-based approach to process synthesis for process intensification. It generates phenomena-based flowsheet options using superstructure optimization and provides a dedicated translation into equipment-based flowsheets. The considered case-study illustrates the application of the method for the analysis of ethyl tert-butyl ether production, based on the conversion of tert-butyl alcohol, under consideration of variable configurations of a rector network and a newly introduced pervaporation-based membrane-reactor block.en0009-286X20193336348Membrane reactorsModelingProcess optimizationSynthesisAllgemeines, WissenschaftJournal Article10.1002/cite.201800119Other