Marco Giulietti
Current Organizations / Institutes
The organizations/institutes from the scholar's latest article
Previous Organizations / Institutes
The organizations / institutes from the scholar's other articles in the past ten years
Marco Giulietti has a total of 13 co-authors. Here are the top co-authors by number of shared publications:
A. B. N. Brito
Federal University of Espírito Santo, Engineering and Computing Dept. - Rodovia BR 101 Norte, Km. 60, Bairro Litorâneo, CEP 29932-540, São Mateus-ES, Brazil
1 shared publicationA. T. C. R. Silva
Federal University of Sao Carlos, Chemical Engineering Department, Industrial Crystallization Laboratory - Rod. Washington Luís km 235, P.O. Box 676, CEP:13565-905, Sao Carlos-SP, Brazil
1 shared publication- André Bernardo
Universidade Federal de Sao Carlos, Brazil
1 shared publication - Antonio Gilberto Ferreira
Departamento de Química, Universidade Federal de Sāo Carlos, Sāo Carlos, Brazil
1 shared publication - C. O. Hokka
Universidade Federal de São Carlos, Brasil
1 shared publication - Caliane Bastos Borba Costa
Universidade Estadual de Maringá, Maringa, Brazil, Brazil
1 shared publication
Latest Publications
- 28 October 2013
- Published by American Chemical Society (ACS) in Journal of Chemical & Engineering Data
- Vol. 58 (11) , 3039-3045
Fructose Solubility in Mixed (Ethanol + Water) Solvent: Experimental Data and Comparison among Different Thermodynamic Models
- 28 October 2013
- Published by American Chemical Society (ACS) in Journal of Chemical & Engineering Data
- Vol. 58 (11) , 3039-3045
Fructose Solubility in Mixed (Ethanol + Water) Solvent: Experimental Data and Comparison among Different Thermodynamic Models
- 1 June 2013
- Published by FapUNIFESP (SciELO) in Brazilian Journal of Chemical Engineering
- Vol. 30 (2) , 231-244
Optimization of the precipitation of clavulanic acid from fermented broth using t-octylamine as intermediate
This work describes the use of clavulanic acid (CA) precipitation as the final step in the process of purification of CA from fermentation broth as an alternative to conventional methods employed traditionally. The purpose of this study was to use a stable intermediate (t-octylamine) between the conversion of CA to its salt form (potassium clavulanate), thereby enabling the resulting intermediate (amine salt of clavulanic acid) to improve the purification process and maintain the stability of the resulting potassium clavulanate. To this end, response surface methodology was employed to optimize the precipitation step. For the first reaction, five temperatures (6.6 to 23.4 ºC), concentrations of clavulanic acid in organic solvent (6.6 to 23.4 mg/mL) and t-octylamine inflow rates (0.33 to 1.17 drop/min) were selected based on a central composite rotatable design (CCRD). For the second reaction, five temperatures (11.6 to 28.4 ºC), concentrations of clavulanic acid amine salt in organic solvent (8.2 to 41.8 mg/mL) and concentrations of potassium 2-ethylhexanoate (0.2 to 1.2 molar) were also selected using CCRD. From these results, precipitation conditions were selected and applied to the purification of CA from the fermentation broth, obtaining a yield of 72.37%.
- 1 June 2013
- Published by FapUNIFESP (SciELO) in Brazilian Journal of Chemical Engineering
- Vol. 30 (2) , 231-244
Optimization of the precipitation of clavulanic acid from fermented broth using t-octylamine as intermediate
This work describes the use of clavulanic acid (CA) precipitation as the final step in the process of purification of CA from fermentation broth as an alternative to conventional methods employed traditionally. The purpose of this study was to use a stable intermediate (t-octylamine) between the conversion of CA to its salt form (potassium clavulanate), thereby enabling the resulting intermediate (amine salt of clavulanic acid) to improve the purification process and maintain the stability of the resulting potassium clavulanate. To this end, response surface methodology was employed to optimize the precipitation step. For the first reaction, five temperatures (6.6 to 23.4 ºC), concentrations of clavulanic acid in organic solvent (6.6 to 23.4 mg/mL) and t-octylamine inflow rates (0.33 to 1.17 drop/min) were selected based on a central composite rotatable design (CCRD). For the second reaction, five temperatures (11.6 to 28.4 ºC), concentrations of clavulanic acid amine salt in organic solvent (8.2 to 41.8 mg/mL) and concentrations of potassium 2-ethylhexanoate (0.2 to 1.2 molar) were also selected using CCRD. From these results, precipitation conditions were selected and applied to the purification of CA from the fermentation broth, obtaining a yield of 72.37%.
- 30 August 2010
- Published by Wiley in Crystal Research and Technology
- Vol. 45 (10) , 1032-1034
Separation of glucose and fructose by freezing crystallization
- 30 August 2010
- Published by Wiley in Crystal Research and Technology
- Vol. 45 (10) , 1032-1034
Separation of glucose and fructose by freezing crystallization