Industrial scale-up of tissue-cultured Dracaena cambodiana Pierre ex Gagnep

Trees ◽  
2022 ◽  
Author(s):  
Feng Zheng ◽  
Yuping Xiong ◽  
Kunlin Wu ◽  
Jaime A. Teixeira da Silva ◽  
Songjun Zeng ◽  
...  
Metabolites ◽  
2022 ◽  
Vol 12 (1) ◽  
pp. 45
Author(s):  
Qi Yang ◽  
Wenli Lin ◽  
Jiawei Xu ◽  
Nan Guo ◽  
Jiachen Zhao ◽  
...  

Bioreactor scale-up from the laboratory scale to the industrial scale has always been a pivotal step in bioprocess development. However, the transition of a bioeconomy from innovation to commercialization is often hampered by performance loss in titer, rate and yield. These are often ascribed to temporal variations of substrate and dissolved oxygen (for instance) in the environment, experienced by microorganisms at the industrial scale. Oscillations in dissolved oxygen (DO) concentration are not uncommon. Furthermore, these fluctuations can be exacerbated with poor mixing and mass transfer limitations, especially in fermentations with filamentous fungus as the microbial cell factory. In this work, the response of glucose-limited chemostat cultures of an industrial Penicillium chrysogenum strain to different dissolved oxygen levels was assessed under both DO shift-down (60% → 20%, 10% and 5%) and DO ramp-down (60% → 0% in 24 h) conditions. Collectively, the results revealed that the penicillin productivity decreased as the DO level dropped down below 20%, while the byproducts, e.g., 6-oxopiperidine-2-carboxylic acid (OPC) and 6-aminopenicillanic acid (6APA), accumulated. Following DO ramp-down, penicillin productivity under DO shift-up experiments returned to its maximum value in 60 h when the DO was reset to 60%. The result showed that a higher cytosolic redox status, indicated by NADH/NAD+, was observed in the presence of insufficient oxygen supply. Consistent with this, flux balance analysis indicated that the flux through the glyoxylate shunt was increased by a factor of 50 at a DO value of 5% compared to the reference control, favoring the maintenance of redox status. Interestingly, it was observed that, in comparison with the reference control, the penicillin productivity was reduced by 25% at a DO value of 5% under steady state conditions. Only a 14% reduction in penicillin productivity was observed as the DO level was ramped down to 0. Furthermore, intracellular levels of amino acids were less sensitive to DO levels at DO shift-down relative to DO ramp-down conditions; this difference could be caused by different timescales between turnover rates of amino acid pools (tens of seconds to minutes) and DO switches (hours to days at steady state and minutes to hours at ramp-down). In summary, this study showed that changes in oxygen availability can lead to rapid metabolite, flux and productivity responses, and dynamic DO perturbations could provide insight into understanding of metabolic responses in large-scale bioreactors.


Technologies ◽  
2020 ◽  
Vol 8 (3) ◽  
pp. 45
Author(s):  
Marilena Radoiu ◽  
Harmandeep Kaur ◽  
Anna Bakowska-Barczak ◽  
Steven Splinter

Cannabis is a flowering plant that has long been used for medicinal, therapeutic, and recreational purposes. Cannabis contains more than 500 different compounds, including a unique class of terpeno-phenolic compounds known as cannabinoids. Δ9-tetrahydrocannabinol (THC) and cannabidiol (CBD) are the most extensively studied cannabinoids. They have been associated with the therapeutic and medicinal properties of the cannabis plant and also with its popularity as a recreational drug. In this paper, an industrial method for cannabis extraction using 915 MHz microwaves coupled with continuous flow operation is presented. The main advantages of the microwave-assisted extraction (MAE) are associated to the continuous-flow operation at atmospheric pressure which allows for higher volumes of biomass to be processed in less time than existing extraction methods, with improved extraction efficiency leading to increased final product yields, improved extract consistency and quality because the process does not require stopping and restarting material flows, and ease of scale-up to industrial scale without the use of pressurised batch vessels. Moreover, due to the flexibility of changing the operation conditions, MAE eliminates additional steps required in most extraction methods, such as biomass decarboxylation or winterisation, which typically adds at least a half day to the extraction process. Another factor that sets MAE apart is the ability to achieve high extraction efficiency, i.e., up to 95% of the active compounds from cannabis biomass can be recovered at industrial scale.


2016 ◽  
Vol 135 ◽  
pp. 1085-1097 ◽  
Author(s):  
Fabiano Piccinno ◽  
Roland Hischier ◽  
Stefan Seeger ◽  
Claudia Som

2005 ◽  
Vol 125 (2) ◽  
pp. 077-098 ◽  
Author(s):  
Nathan S. Mosier ◽  
Richard Hendrickson ◽  
Mark Brewer ◽  
Nancy Ho ◽  
Miroslav Sedlak ◽  
...  

2005 ◽  
Vol 28 (12-13) ◽  
pp. 1877-1891 ◽  
Author(s):  
Ian Sutherland ◽  
David Hawes ◽  
Svetlana Ignatova ◽  
Lee Janaway ◽  
Philip Wood
Keyword(s):  
Scale Up ◽  

1990 ◽  
Vol 55 (7) ◽  
pp. 1730-1740 ◽  
Author(s):  
Petr Ettler

Our philosophy of successful biotechnology transfer to industrial scale covers the comparison of complex sets of microbiological, analytical and bioengineering data from cultivations in various scales and different geometries of mixing with laboratory findings. In particular, the availability of nutrients to producing microorganism should be understood, therefore for quick scaling-up procedure of polyene antibiotics produced by Streptomyces noursei we recommend to use physiological marker as total dehydrogenase activity determination. The utility of scale-down tests for identification of process fluctuation, validation of new substrate batches and simultaneous control of inoculum quality was proved.


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