Salting-out assisted solvent extraction of L (+) lactic acid obtained after fermentation of sugarcane bagasse hydrolysate

Author(s):  
Pratibha Baral ◽  
Anushka Pundi ◽  
Akhilesh Kumar ◽  
Raghuvir Singh ◽  
Vinod Kumar ◽  
...  
2014 ◽  
Vol 931-932 ◽  
pp. 1597-1601 ◽  
Author(s):  
Woranart Jonglertjunya ◽  
Nattawee Srimarut ◽  
Nawapol Lukkanakul ◽  
Chularat Sakdaronnarong ◽  
Norased Nasongkla

Delignified sugarcane bagasse (SCB) by solvent extraction was carried out at moderate condition (90°C, 4 h) in the presence of acid catalyst. To investigate the dissolution of lignin into solvent, different solvents were utilized during lignin extraction process. Delignified SCB was further hydrolyzed by cell wall degrading enzyme complexes prior to sugar determination. The results showed that n-butanol was the most promising solvent enhancing lignin dissolution which in turn led to highest yield of glucose (63.1% based on treated SCB) and no xylose was detected in hydrolysate. The lignin extraction by n-butanol in the presence of H2SO4 and subsequent saccharification process were then scaled up for lactic acid production. The maximum lactic acid was obtained at 25.7 ± 0.2 g/l from L. casei fermentation after 96 hours when sugarcane bagasse hydrolysate containing 25.6±1.4 g/l initial glucose concentration was used as substrate.


2021 ◽  
Vol 72 (3) ◽  
pp. 102-111
Author(s):  
Jamal Stas ◽  
Marwa Yousef

The aim of this paper is to investigate the possibility to recover lactic acid (LA) from the whey of yoghurt by easy and effective solvent extraction technique using tri-n-octylamine, tri-n-butyl phosphate, and their mixtures as extractant. All parameters affecting the transfer of lactic acid to the organic phase were investigated including: time of stirring, tri-n-butyl phosphate and tri-n- octylamine concentrations, organic to aqueous phase ratio, temperature, NaCl concentration as a salting out agent, and number of contacts. The maximum yield of LA extraction can be obtained by using the following operation conditions: 0.8M TOA+11% TBP, Vorg/Vaq = 4/1, t = 30 oC, [NaCl] = 2M. Complete stripping of LA from loaded organic phase can be done in 2 stages using double distilled water at 60oC and Vaq/Vorg = 20/1.


2021 ◽  
Vol 170 ◽  
pp. 107021
Author(s):  
Rafael de Carvalho Gomes ◽  
Lídia Yokoyama ◽  
Ysrael Marrero Vera

Fuel ◽  
2019 ◽  
Vol 254 ◽  
pp. 115653 ◽  
Author(s):  
Sheetal Bandhu ◽  
Neha Bansal ◽  
Diptarka Dasgupta ◽  
Vivek Junghare ◽  
Arushdeep Sidana ◽  
...  

2019 ◽  
Vol 39 (2) ◽  
Author(s):  
Maleeha Manzoor ◽  
Qurat‐ul‐Ain Ahmad ◽  
Ambreen Aslam ◽  
Faiza Jabeen ◽  
Azhar Rasul ◽  
...  

Author(s):  
Ketaki Nalawade ◽  
Paharika Saikia ◽  
Shuvashish Behera ◽  
Kakasaheb Konde ◽  
Sanjay Patil

2020 ◽  
Vol 124 ◽  
pp. 72-81
Author(s):  
Pratibha Baral ◽  
Anushka Pundir ◽  
Vinod Kumar ◽  
Akhilesh K. Kurmi ◽  
Deepti Agrawal

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