scholarly journals Lactic acid recovery from a model of Thermotoga neapolitana fermentation broth using ion exchange resins in batch and fixed-bed reactors

2018 ◽  
Vol 54 (6) ◽  
pp. 1008-1025 ◽  
Author(s):  
Vincenzo Luongo ◽  
Angelo Palma ◽  
Eldon R. Rene ◽  
Angelo Fontana ◽  
Francesco Pirozzi ◽  
...  
2021 ◽  
Vol 18 (2) ◽  
pp. 9-14
Author(s):  
Carlos Jacinto ◽  
Erick Ramos ◽  
Dora López

Un método de adsorción utilizando la resina Dowex™Marathon™ WBA ha sido desarrollado con el fin de evaluar larecuperación de ácido cítrico producido por fermentación sumergida. Para determinar la viabilidad de este método de separación, la resina fue evaluada a diferentes condiciones de temperatura (30 – 70 °C) y pH (1.5 – 6.5). Los resultadosmostraron que a pH bajo, se mejora la adsorción de ácido cítrico, a través de la cual, se recupera el 85% del ácido y se obtiene una pureza del 92%. Esto representa una capacidad máxima de adsorción de 0.46 g de ácido cítrico por gramo de resina empleada.


2009 ◽  
Vol 17 (5) ◽  
pp. 773-780 ◽  
Author(s):  
Yixin QU ◽  
Shaojun PENG ◽  
Shui WANG ◽  
Zhiqiang ZHANG ◽  
Jidong WANG

2021 ◽  
Vol 22 ◽  
pp. 101438
Author(s):  
Ashfaq Ahmad ◽  
Israa Othman ◽  
Hanifa Taher ◽  
Fawzi Banat

2021 ◽  
Vol 8 (1) ◽  
Author(s):  
Nur Akmal Solehah Din ◽  
Seng Joe Lim ◽  
Mohamad Yusof Maskat ◽  
Sahilah Abd Mutalib ◽  
Nurul Aqilah Mohd Zaini

AbstractLactic acid has become one of the most important chemical substances used in various sectors. Its global market demand has significantly increased in recent years, with a CAGR of 18.7% from 2019 to 2025. Fermentation has been considered the preferred method for producing high-purity lactic acid in the industry over chemical synthesis. However, the recovery and separation of lactic acid from microbial fermentation media are relatively complicated and expensive, especially in the process relating to second-generation (2G) lactic acid recovery. This article reviews the development and progress related to lactic acid separation and recovery from fermentation broth. Various aspects are discussed thoroughly, such as the mechanism of lactic acid production through fermentation, the crucial factors that influence the fermentation process, and the separation and recovery process of conventional and advanced lactic acid separation methods. This review's highlight is the recovery of lactic acid by adsorption technique using ion-exchange resins with a brief focus on the potential of in-site separation strategies alongside the important factors that influenced the lactic acid recovery process by ion exchange. Apart from that, other lactic acid separation techniques, such as chemical neutralization, liquid–liquid extraction, membrane separation, and distillation, are also thoroughly reviewed.


2006 ◽  
Vol 45 (9) ◽  
pp. 3243-3247 ◽  
Author(s):  
M. Isabel González ◽  
Silvia Álvarez ◽  
Francisco A. Riera ◽  
Ricardo Álvarez

Water ◽  
2021 ◽  
Vol 13 (11) ◽  
pp. 1572
Author(s):  
X. Vecino ◽  
M. Reig ◽  
C. Valderrama ◽  
J. L. Cortina

The downstream processing for the separation and purification of lactic acid is a hot research area in the bio-refinery field due to its continuous growing market in different sectors, such as the food, cosmetic and pharmaceutical sectors. In this work, the use of ion-exchange technology for lactic acid recovery is proposed. For that, four anion exchange resins with different polymer structures and functional groups were tested (A100, MN100, A200E and MP64). The sorption process was optimized by the Box–Behnken factorial design, and the experimental data obtained in the sorption process were analyzed by using the response surface methodology and fitted at different isotherms and kinetics models. Moreover, regenerant type, contact time and solid/liquid ratio were evaluated in the desorption process. Results showed that the best resin for lactic acid removal was A100, at pH = 4, with a resin/lactic acid solution ratio of 0.15 g/mL during a maximum of 1 h, achieving 85% of lactic acid removal. Moreover, equilibrium data sorption of lactic acid onto A100 resin was fitted by a Langmuir isotherm and by a kinetic model of a pseudo-second order. In addition, in the desorption process, it was stablished that a resin/regenerant ratio of 0.15 g/mL during 30 min with 0.1 M of NaOH solution provided the best results (4.45 ± 0.08 mg/g).


Sign in / Sign up

Export Citation Format

Share Document