### Abstract

A procedure for the simulation of extraction columns is developed using a program, Thermath, based on the Mathematica® computer algebra (CA) software. The procedure requires the simultaneous solution, using the Newton-Raphson method, of mass and energy balances, phase equilibrium equations, and equations needed to match the number of degrees of freedom at each stage. Starting from the equipment model equations, analytical derivatives with respect to the problem unknowns were obtained using CA, and automatically implemented in FORTRAN using Thermath. Similarly, fugacity coefficients and residual enthalpies were derived from the Peng-Robinson and the Soave-Redlich-Kwong equations of state, using either the classical or the Huron-Vidal mixing rules, and also implemented using Thermath. The code was used to simulate the separation of products from an enzymatic reaction using supercritical carbon dioxide. Extraction columns for the systems carbon dioxide-ethanol-water and carbon dioxide-limonene-linalool were also simulated. The results show trends compatible with those that should be expected from supercritical extraction columns.

Original language | English |
---|---|

Pages (from-to) | 203-208 |

Number of pages | 6 |

Journal | Journal of Supercritical Fluids |

Volume | 34 |

Issue number | 2 SPEC. ISS. |

DOIs | |

Publication status | Published - Jun 2005 |

Externally published | Yes |

### Fingerprint

### Keywords

- Computer algebra
- Equations of state
- Extraction columns
- Mathematica®
- Supercritical fluids

### ASJC Scopus subject areas

- Physical and Theoretical Chemistry
- Materials Science (miscellaneous)
- Physics and Astronomy (miscellaneous)

### Cite this

*Journal of Supercritical Fluids*,

*34*(2 SPEC. ISS.), 203-208. https://doi.org/10.1016/j.supflu.2004.11.015

**Modeling and simulation of supercritical extraction columns using computer algebra.** / Nogueira, Bianca M M; Alfradique, Marcelo F.; Castier, Marcelo.

Research output: Contribution to journal › Article

*Journal of Supercritical Fluids*, vol. 34, no. 2 SPEC. ISS., pp. 203-208. https://doi.org/10.1016/j.supflu.2004.11.015

}

TY - JOUR

T1 - Modeling and simulation of supercritical extraction columns using computer algebra

AU - Nogueira, Bianca M M

AU - Alfradique, Marcelo F.

AU - Castier, Marcelo

PY - 2005/6

Y1 - 2005/6

N2 - A procedure for the simulation of extraction columns is developed using a program, Thermath, based on the Mathematica® computer algebra (CA) software. The procedure requires the simultaneous solution, using the Newton-Raphson method, of mass and energy balances, phase equilibrium equations, and equations needed to match the number of degrees of freedom at each stage. Starting from the equipment model equations, analytical derivatives with respect to the problem unknowns were obtained using CA, and automatically implemented in FORTRAN using Thermath. Similarly, fugacity coefficients and residual enthalpies were derived from the Peng-Robinson and the Soave-Redlich-Kwong equations of state, using either the classical or the Huron-Vidal mixing rules, and also implemented using Thermath. The code was used to simulate the separation of products from an enzymatic reaction using supercritical carbon dioxide. Extraction columns for the systems carbon dioxide-ethanol-water and carbon dioxide-limonene-linalool were also simulated. The results show trends compatible with those that should be expected from supercritical extraction columns.

AB - A procedure for the simulation of extraction columns is developed using a program, Thermath, based on the Mathematica® computer algebra (CA) software. The procedure requires the simultaneous solution, using the Newton-Raphson method, of mass and energy balances, phase equilibrium equations, and equations needed to match the number of degrees of freedom at each stage. Starting from the equipment model equations, analytical derivatives with respect to the problem unknowns were obtained using CA, and automatically implemented in FORTRAN using Thermath. Similarly, fugacity coefficients and residual enthalpies were derived from the Peng-Robinson and the Soave-Redlich-Kwong equations of state, using either the classical or the Huron-Vidal mixing rules, and also implemented using Thermath. The code was used to simulate the separation of products from an enzymatic reaction using supercritical carbon dioxide. Extraction columns for the systems carbon dioxide-ethanol-water and carbon dioxide-limonene-linalool were also simulated. The results show trends compatible with those that should be expected from supercritical extraction columns.

KW - Computer algebra

KW - Equations of state

KW - Extraction columns

KW - Mathematica®

KW - Supercritical fluids

UR - http://www.scopus.com/inward/record.url?scp=15744383913&partnerID=8YFLogxK

UR - http://www.scopus.com/inward/citedby.url?scp=15744383913&partnerID=8YFLogxK

U2 - 10.1016/j.supflu.2004.11.015

DO - 10.1016/j.supflu.2004.11.015

M3 - Article

AN - SCOPUS:15744383913

VL - 34

SP - 203

EP - 208

JO - Journal of Supercritical Fluids

JF - Journal of Supercritical Fluids

SN - 0896-8446

IS - 2 SPEC. ISS.

ER -