Development of a Continuous Aqueous Two-phase Flotation Process for the Downstream Processing of Biotechnological Products

Author(s):  
Lucas Jakob ◽  
Marcel Heinzmann ◽  
Hermann Nirschl
2015 ◽  
Vol 2 (1) ◽  
pp. 39-48 ◽  
Author(s):  
M.C Madhusudhan ◽  
N. Amrutha ◽  
Anupama Rani ◽  
KSMS Raghavarao

2013 ◽  
Vol 101 ◽  
pp. 392-397 ◽  
Author(s):  
Luis V. Rodríguez-Durán ◽  
Darío Spelzini ◽  
Valeria Boeris ◽  
Cristóbal N. Aguilar ◽  
Guillermo A. Picó

2015 ◽  
Vol 1383 ◽  
pp. 35-46 ◽  
Author(s):  
Christopher Ladd Effio ◽  
Lukas Wenger ◽  
Ozan Ötes ◽  
Stefan A. Oelmeier ◽  
Richard Kneusel ◽  
...  

AMB Express ◽  
2021 ◽  
Vol 11 (1) ◽  
Author(s):  
Miguel Flores-Gatica ◽  
Héctor Castañeda-Aponte ◽  
Mónica Rebeca Gil-Garzon ◽  
Liliana Monserrath Mora-Galvez ◽  
Martin Paul Banda-Magaña ◽  
...  

AbstractGiven its biocompatibility, rheological, and physiological properties, hyaluronic acid (HA) has become a biomaterial of increasing interest with multiple applications in medicine and cosmetics. In recent decades, microbial fermentations have become an important source for the industrial production of HA. However, due to its final applications, microbial HA must undergo critical and long purification processes to ensure clinical and cosmetic grade purity. Aqueous two-phase systems (ATPS) have proven to be an efficient technique for the primary recovery of high-value biomolecules. Nevertheless, their implementation in HA downstream processing has been practically unexplored. In this work, polyethylene glycol (PEG)–citrate ATPS were used for the first time for the primary recovery of HA produced with an engineered strain of Streptococcus equi subsp. zooepidemicus. The effects of PEG molecular weight (MW), tie-line length (TLL), volume ratio (VR), and sample load on HA recovery and purity were studied with a clarified fermentation broth as feed material. HA was recovered in the salt-rich bottom phase, and its recovery increased when a PEG MW of 8000 g mol−1 was used. Lower VR values (0.38) favoured HA recovery, whereas purity was enhanced by a high VR (3.50). Meanwhile, sample load had a negative impact on both recovery and purity. The ATPS with the best performance was PEG 8000 g mol−1, TLL 43% (w/w), and VR 3.50, showing 79.4% HA recovery and 74.5% purity. This study demonstrated for the first time the potential of PEG–citrate ATPS as an effective primary recovery strategy for the downstream process of microbial HA.


2012 ◽  
Vol 47 (9) ◽  
pp. 1358-1363 ◽  
Author(s):  
B.S. Priyanka ◽  
Navin K. Rastogi ◽  
K.S.M.S. Raghavarao ◽  
M.S. Thakur

2013 ◽  
Vol 2013 ◽  
pp. 1-18 ◽  
Author(s):  
Mayank Saraswat ◽  
Luca Musante ◽  
Alessandra Ravidá ◽  
Brian Shortt ◽  
Barry Byrne ◽  
...  

Advances in fermentation technologies have resulted in the production of increased yields of proteins of economic, biopharmaceutical, and medicinal importance. Consequently, there is an absolute requirement for the development of rapid, cost-effective methodologies which facilitate the purification of such products in the absence of contaminants, such as superfluous proteins and endotoxins. Here, we provide a comprehensive overview of a selection of key purification methodologies currently being applied in both academic and industrial settings and discuss how innovative and effective protocols such as aqueous two-phase partitioning, membrane chromatography, and high-performance tangential flow filtration may be applied independently of or in conjunction with more traditional protocols for downstream processing applications.


1997 ◽  
Vol 32 (8) ◽  
pp. 635-641 ◽  
Author(s):  
S. Tanuja ◽  
N.D. Srinivas ◽  
K.S.M.S. Raghava Rao ◽  
M.K. Gowthaman

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