In this paper substance transfer phenomena in the multistage reactive system were investigated.Substance transfer between liquid and gas phases in a distillation packed column with reactionesterification was examined. Efficiency of substance transfer were examined by HTU-Height of transferunits and volumetric substance transfer coefficients. The esterification reaction of the ethanol andacetic acid was examined. Based on derived mathematical model the total height of transfer units andindividual height of transfer units for the liquid and gas phases were determined. The investigation wasperformed by computer simulation and experiments. Several correlation models for HTU/NTU andsubstance transfer coefficients were studied. The correlations f...
Gas-liquid-liquid reactions play a significant role in the field of chemical process technology, how...
An absorption model has been developed which is able to calculate the simultaneous absorption rates ...
The design and operation issues for reactive distillation systems are considerably more complex than...
In this paper substance transfer phenomena in the multistage reactive system were investigated.Subst...
In this paper substance transfer rate in the multistage system was investigated. Substance transfer ...
A multistage distillation column in which mass transfer and a reversible chemical reaction occurred ...
In many processes in the chemical industry mass transfer accompanied with reversible, complex chemic...
A cascade model including the Stefan-Maxwell model for mass transfer is developed to assess the feas...
An absorption model to study gas–liquid mass transfer accompanied by reversible two-step reactions i...
An absorption model to study gas–liquid mass transfer accompanied by reversible two-step reactions i...
Gas-liquid-liquid reaction systems may be encountered in several important fields of application as ...
In many processes in the chemical industry mass transfer accompanied with reversible, complex chemic...
ln many processes in tbe the chemical industry mass transfer accompanied with reversible, complex ch...
An absorption model to study gas–liquid mass transfer accompanied by reversible two-step reactions i...
The effect of mass transfer on feasible products is analyzed for two industrially relevant classes o...
Gas-liquid-liquid reactions play a significant role in the field of chemical process technology, how...
An absorption model has been developed which is able to calculate the simultaneous absorption rates ...
The design and operation issues for reactive distillation systems are considerably more complex than...
In this paper substance transfer phenomena in the multistage reactive system were investigated.Subst...
In this paper substance transfer rate in the multistage system was investigated. Substance transfer ...
A multistage distillation column in which mass transfer and a reversible chemical reaction occurred ...
In many processes in the chemical industry mass transfer accompanied with reversible, complex chemic...
A cascade model including the Stefan-Maxwell model for mass transfer is developed to assess the feas...
An absorption model to study gas–liquid mass transfer accompanied by reversible two-step reactions i...
An absorption model to study gas–liquid mass transfer accompanied by reversible two-step reactions i...
Gas-liquid-liquid reaction systems may be encountered in several important fields of application as ...
In many processes in the chemical industry mass transfer accompanied with reversible, complex chemic...
ln many processes in tbe the chemical industry mass transfer accompanied with reversible, complex ch...
An absorption model to study gas–liquid mass transfer accompanied by reversible two-step reactions i...
The effect of mass transfer on feasible products is analyzed for two industrially relevant classes o...
Gas-liquid-liquid reactions play a significant role in the field of chemical process technology, how...
An absorption model has been developed which is able to calculate the simultaneous absorption rates ...
The design and operation issues for reactive distillation systems are considerably more complex than...