Optimal design and operation of multivessel batch distillation with fixed product demand. Modelling, simulation and optimisation of design and operation parameters in multivessel batch distillation under fixed product demand scenario and strict product specifications using simple dynamic model in gPROMS.
SupervisorMujtaba, Iqbal M.
KeywordConventional batch distillation
Multivessel batch distillation
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InstitutionUniversity of Bradford
DepartmentSchool of Engineering, Design and Technology