Abstract
A mathematical model is presented for steady-state simulation of multiple-effects evaporators systems used for concentration of sugar solution. The model basis are the fundamental energy and mass balances equations, as well as empirical correlations for the problem being handled. The evaporation system simulation is performed with an executive program which allows different process configurations. For one typical case, some process parameters (volumetric rate and concentration of feed;exhaust steam temperature) influences on syrup concentration and solution temperature were studied. (author) 8 figs., 2 refs.
Chiappetta, A;
Giudici, R;
Nascimento, C A.O. do
[1]
- Sao Paulo Univ., SP (Brazil). Escola Politecnica
Citation Formats
Chiappetta, A, Giudici, R, and Nascimento, C A.O. do.
Mathematical modelling and simulation of the operation in sugar and alcohol industry: 2 - evaporation; Modelagem matematica e simulacao das operacoes da industria de acucar e alcool: 2 - evaporacao.
Brazil: N. p.,
1986.
Web.
Chiappetta, A, Giudici, R, & Nascimento, C A.O. do.
Mathematical modelling and simulation of the operation in sugar and alcohol industry: 2 - evaporation; Modelagem matematica e simulacao das operacoes da industria de acucar e alcool: 2 - evaporacao.
Brazil.
Chiappetta, A, Giudici, R, and Nascimento, C A.O. do.
1986.
"Mathematical modelling and simulation of the operation in sugar and alcohol industry: 2 - evaporation; Modelagem matematica e simulacao das operacoes da industria de acucar e alcool: 2 - evaporacao."
Brazil.
@misc{etde_666305,
title = {Mathematical modelling and simulation of the operation in sugar and alcohol industry: 2 - evaporation; Modelagem matematica e simulacao das operacoes da industria de acucar e alcool: 2 - evaporacao}
author = {Chiappetta, A, Giudici, R, and Nascimento, C A.O. do}
abstractNote = {A mathematical model is presented for steady-state simulation of multiple-effects evaporators systems used for concentration of sugar solution. The model basis are the fundamental energy and mass balances equations, as well as empirical correlations for the problem being handled. The evaporation system simulation is performed with an executive program which allows different process configurations. For one typical case, some process parameters (volumetric rate and concentration of feed;exhaust steam temperature) influences on syrup concentration and solution temperature were studied. (author) 8 figs., 2 refs.}
journal = []
issue = {5}
volume = {9}
journal type = {AC}
place = {Brazil}
year = {1986}
month = {Dec}
}
title = {Mathematical modelling and simulation of the operation in sugar and alcohol industry: 2 - evaporation; Modelagem matematica e simulacao das operacoes da industria de acucar e alcool: 2 - evaporacao}
author = {Chiappetta, A, Giudici, R, and Nascimento, C A.O. do}
abstractNote = {A mathematical model is presented for steady-state simulation of multiple-effects evaporators systems used for concentration of sugar solution. The model basis are the fundamental energy and mass balances equations, as well as empirical correlations for the problem being handled. The evaporation system simulation is performed with an executive program which allows different process configurations. For one typical case, some process parameters (volumetric rate and concentration of feed;exhaust steam temperature) influences on syrup concentration and solution temperature were studied. (author) 8 figs., 2 refs.}
journal = []
issue = {5}
volume = {9}
journal type = {AC}
place = {Brazil}
year = {1986}
month = {Dec}
}