The design and operation issues for reactive distillation systems are considerably more
complex than those involved for either conventional reactors or conventional distillation …

Distillation and absorption are well-known separation processes that quite often can be
designed using the concept of theoretical stages. The distillation of wide boiling systems, as …

In this research, a nonequilibrium dynamic stage model has been developed for reactive
absorption of carbon dioxide by carbonated ammonia solutions. The model considers mass …

An extensive set of experimental data on multicomponent distillation with non-ideal systems
in structured packed columns is presented to fill the gap of such data in literature …

Dealing with complex process units like dividing wall columns pushes the focus on the
determination of suitable modelling approaches. For this purpose a nonequilibrium stage …

Dynamic rate‐based approach for modeling and simulating batch distillation is presented.
To predict separation efficiencies, mass transfer was considered explicitly using the Maxwell …

In this thesis a nonequilibrium (NEQ) cell model is developed to describe the dynamic
operation of reactive distillation (RD) tray columns. The features of the model are:(1) use of …

A dynamic, nonisothermal, nonequilibrium model is developed to predict detailed transient
behavior during startup and transition to standby for concentrated random-packed …

Packed distillation and absorption columns are often modeled using equilibrium stages.
However, determination of the packing height that corresponds to an equilibrium stage is not …

Reactive distillation is an integrated process which considers simultaneous physical and
chemical transformations. It is increasingly receiving attention both from industry and …