Advanced search
Start date
Betweenand
(Reference retrieved automatically from Web of Science through information on FAPESP grant and its corresponding number as mentioned in the publication by the authors.)

A new unified model to simulate columns with multiple phase divisions and their impact on energy savings

Full text
Author(s):
Biasi, Lilian C. K. [1] ; Heinkenschloss, Matthias [2] ; Batista, Fabio R. M. [3] ; Zemp, Roger J. [4, 5] ; Romano, Ana L. R. [1] ; Meirelles, Antonio J. A. [1]
Total Authors: 6
Affiliation:
[1] Univ Estadual Campinas, Sch Food Engn, Dept Food Engn, UNICAMP, Lab Extract Appl Thermodynam & Equilibrium, ExTrAE, BR-13083862 Campinas, SP - Brazil
[2] Rice Univ, Dept Computat & Appl Math, Houston, TX 77005 - USA
[3] Univ Sao Paulo, Sch Engn Lorena, Dept Chem Engn, BR-2602810 Lorena, SP - Brazil
[4] Univ Estadual Campinas, Dept Chem Syst Engn, UNICAMP, BR-13083862 Campinas, SP - Brazil
[5] Univ Estadual Campinas, Sch Chem Engn, UNICAMP, BR-13083862 Campinas, SP - Brazil
Total Affiliations: 5
Document type: Journal article
Source: Computers & Chemical Engineering; v. 140, SEP 2 2020.
Web of Science Citations: 0
Abstract

This paper presents a new unified model that allows the simulation of distillation columns with any integer number of phase divisions. Such columns have the potential for substantial savings in energy and capital costs. However, conventional simulators do not cover columns with phase divisions and previous simulations required a tailored algorithm for each type of column. The proposed model uses a unique set of MESH-equations for parastillation, metastillation, and conventional distillation. With small modifications in the stage indexing, the model allows the simulation of conventional, top and bottom-DWCs. This generalization was possible by introducing two new variables: the number of liquid (theta) and vapor (beta) phase divisions. The positive impact of increasing the number of phase divisions was demonstrated in the bioethanol distillation, by analyzing parastillation and metastillation columns. These columns reduce the operational and total annual costs in 19% and 15%, when compared to conventional columns. (C) 2020 Elsevier Ltd. All rights reserved. (AU)

FAPESP's process: 14/21252-0 - Equilibrium and production processes of biofuels and bioproducts
Grantee:Antonio José de Almeida Meirelles
Support Opportunities: Research Projects - Thematic Grants
FAPESP's process: 16/10636-8 - From the cell factory to the Biodiesel-Bioethanol integrated biorefinery: a systems approach applied to complex problems in micro and macroscales
Grantee:Roberto de Campos Giordano
Support Opportunities: Program for Research on Bioenergy (BIOEN) - Thematic Grants