Repository logo
Log In(current)
  • Inicio
  • Personal de Investigación
  • Unidad Académica
  • Publicaciones
  • Colecciones
    Datos de Investigacion Divulgacion cientifica Personal de Investigacion Protecciones Proyectos Externos Proyectos Internos Publicaciones Tesis
  1. Home
  2. Universidad de Santiago de Chile
  3. Publicaciones ANID
  4. Effect of the Operating Variables on the Extraction and Recovery of Aroma Compounds in an Osmotic Distillation Process Coupled to a Vacuum Membrane Distillation System
Details

Effect of the Operating Variables on the Extraction and Recovery of Aroma Compounds in an Osmotic Distillation Process Coupled to a Vacuum Membrane Distillation System

Journal
Journal of Food Engineering
ISSN
0260-8774
Date Issued
2012
Author(s)
Romero-Figueroa, J  
Torres-Mediano, A  
Plaza, A  
DOI
https://doi.org/10.1016/j.jfoodeng.2012.03.004
Abstract
The coupled operation of osmotic distillation (OD) and vacuum membrane distillation (VMD) for concentration of fruit juices and simultaneous recovery of their aroma compounds was studied. The simulated aqueous fruit juices containing four common aroma compounds were concentrated using osmotic distillation where the feed solution was in contact with a brine solution of CaCl 2, through a hydrophobic macroporous membrane contactor. Aroma compounds absorbed in the extraction brine were extracted using a membrane evaporator under vacuum and collected into a cold trap. This way, both concentration and aroma recovery of fruit juices were achieved simultaneously using two hollow fiber membrane modules. The transfer of the aroma compounds was evaluated by using different operating variables such as hydrodynamic conditions, brine concentration and vacuum pressure. The experiments show that the loss of aroma compounds during the concentration processes can be avoided by means of extraction of the aroma compounds from the brine separately, resulting in an average of 75% recovery in aroma compounds. In general, the process of aroma removal and recovery is faster than the concentration process of the fruit juices by osmotic distillation at a technical and commercial level (higher than 45°Brix). Thus, the simultaneous operation of these two membrane processes can be used to decrease the energy requirements for a given production capacity. © 2012 Elsevier Ltd. All rights reserved.
Get Involved!
  • Source Code
  • Documentation
  • Slack Channel
Make it your own

DSpace-CRIS can be extensively configured to meet your needs. Decide which information need to be collected and available with fine-grained security. Start updating the theme to match your Institution's web identity.

Need professional help?

The original creators of DSpace-CRIS at 4Science can take your project to the next level, get in touch!

Logo USACH

Universidad de Santiago de Chile
Avenida Libertador Bernardo O'Higgins nº 3363. Estación Central. Santiago Chile.
ciencia.abierta@usach.cl © 2023
The DSpace CRIS Project - Modificado por VRIIC USACH.

  • Accessibility settings
  • Privacy policy
  • End User Agreement
  • Send Feedback
Logo DSpace-CRIS
Repository logo COAR Notify