It is difficult to recover trifluoroacetic acid (TFA) from its dilute aqueous solutions by conventional techniques. This work investigates the feasibility of using reactive distillation to recover TFA through esterification with 2-propanol. A kinetic model is proposed based on batch reactor data. Experiments performed using reactive distillation in batch and continuous modes, show significant recovery. Independent column simulations, based on kinetics and vapor–liquid equilibrium (VLE) developed in this work, agree well with our experimental results. The validated model is further used to obtain suitable design and operating parameters to give nearly complete recovery. A complete process recovery process sheet is suggested based on the resu...
Residue curve maps are theoretically generated to assess the feasibility of a reactive distillation ...
Fusel oil is a mixture of C2-C5 alcohols such as ethanol, n-propanol, iso-butanol and iso-amyl alcoh...
Reactive distillation is the combination of unit operations reactor and distillation column into one...
The recovery of acetic acid by reactive distillation through esterification with methanol in the pre...
Lactic acid, being virtually a non-boiling compound, is difficult to separate from its aqueous solut...
With ever-growing environmental concerns, petrochemical and fine chemical industries face an omnipre...
Esterification of lactic acid with n-butanol may be performed to synthesize n-butyl lactate or to re...
Raul LoboTrifluoroacetic anhydride (TFA anhydride) is an important reagent for the production of a n...
International audienceThe glycerol oxidation reaction was developed leading to selective catalysts a...
Abstract This paper addresses an industrially important problem of acetic acid recovery from a waste...
Wastewater containing 2-20wt% of acrylic acid (AA) is currently burned using incinerator which is ne...
The paper presents a parametric study for the design of a reactive distillation column used to recov...
This paper addresses an industrially important problem of acetic acid recovery from a waste water st...
Reactive extraction is an important recovery method for extraction of propionic acid from dilute str...
Esterification reactions are limited by chemical equilibrium and therefore they are carried out com...
Residue curve maps are theoretically generated to assess the feasibility of a reactive distillation ...
Fusel oil is a mixture of C2-C5 alcohols such as ethanol, n-propanol, iso-butanol and iso-amyl alcoh...
Reactive distillation is the combination of unit operations reactor and distillation column into one...
The recovery of acetic acid by reactive distillation through esterification with methanol in the pre...
Lactic acid, being virtually a non-boiling compound, is difficult to separate from its aqueous solut...
With ever-growing environmental concerns, petrochemical and fine chemical industries face an omnipre...
Esterification of lactic acid with n-butanol may be performed to synthesize n-butyl lactate or to re...
Raul LoboTrifluoroacetic anhydride (TFA anhydride) is an important reagent for the production of a n...
International audienceThe glycerol oxidation reaction was developed leading to selective catalysts a...
Abstract This paper addresses an industrially important problem of acetic acid recovery from a waste...
Wastewater containing 2-20wt% of acrylic acid (AA) is currently burned using incinerator which is ne...
The paper presents a parametric study for the design of a reactive distillation column used to recov...
This paper addresses an industrially important problem of acetic acid recovery from a waste water st...
Reactive extraction is an important recovery method for extraction of propionic acid from dilute str...
Esterification reactions are limited by chemical equilibrium and therefore they are carried out com...
Residue curve maps are theoretically generated to assess the feasibility of a reactive distillation ...
Fusel oil is a mixture of C2-C5 alcohols such as ethanol, n-propanol, iso-butanol and iso-amyl alcoh...
Reactive distillation is the combination of unit operations reactor and distillation column into one...