Experimental and numerical investigation of the scale‐up criterion of solid‐viscous fluid mixing in a stirred tank

Author(s):  
Daiqi Lin ◽  
Hongyuan Wei ◽  
Erjia Song ◽  
Boonho Ng ◽  
Ting He ◽  
...  
Author(s):  
Mengxue Zhang ◽  
Yinyu Hu ◽  
Wentan Wang ◽  
Ting Shao ◽  
Yi Cheng

Author(s):  
Mariana Petronela Hanga ◽  
Fritz Anthony Raga ◽  
Panagiota Moutsatsou ◽  
Christopher J. Hewitt ◽  
Alvin W. Nienow ◽  
...  

2014 ◽  
Vol 8 (4) ◽  
pp. 503-517 ◽  
Author(s):  
A. A. Alleyne ◽  
S. Xanthos ◽  
K. Ramalingam ◽  
K. Temel ◽  
H. Li ◽  
...  

Author(s):  
Lei Wang ◽  
Xiao Xu ◽  
Hualin Wang ◽  
HongLai Liu ◽  
Qiang Yang

A gas-liquid stirred tank reactor (STR) has some problems, such as low mass transfer efficiency, high exhaust gas oxygen concentration, and low product conversion rate, due to limitations of stirring speed and input power. This article proposes a method to enhance the gas-liquid mass transfer in a STR using circulating jet internals. When a circulating jet is added, the average bubble size in the reactor is reduced to 1.26 mm, and the overall gas holdup is increased to 8.23%, which is an increase of 3.62 times of the original STR. The gas-liquid volumetric mass transfer coefficient is increased to 0.05556 s-1, which is 4.84 times of the original STR. The unit volume power is increased by only 1.4 times. These data provide references for the design and scale-up of new jet STRs.


2001 ◽  
Vol 47 (4) ◽  
pp. 277-282 ◽  
Author(s):  
Yuxin Wang ◽  
Rafael Vazquez-Duhalt ◽  
Michael A Pickard

We were looking for a strain of Bjerkandera adusta that produces high titres of manganese peroxidase under optimal conditions for large-scale enzyme purification. We have chosen two strains from the University of Alberta Microfungus Collection and Herbarium, UAMH 7308 and 8258, and compared the effects of growth conditions and medium composition on enzyme production with the well-characterized strain BOS55 (ATCC 90940). Of four types of cereal bran examined, rice bran at 3% (w/v) in 60 mM phosphate buffer pH 6 supported the highest levels of enzyme production. Using 100 mL medium in 500-mL Erlenmeyer flasks, maximum enzyme levels in the culture supernatant occurred after about 10 days of growth; 5.5 U·mL–1 for UAMH 7308, 4.4 U·mL–1 for UAMH 8258, and 1.7 U·mL–1 for BOS55, where units are expressed as micromoles of Mn-malonate formed per minute. Growth as submerged cultures in 10-L stirred tank reactors produced 3.5 U·mL–1 of manganese peroxidase (MnP) by UAMH 8258 and 2.5 U·mL–1 of MnP by 7308, while enzyme production by BOS55 was not successful in stirred tank reactors but could be scaled up in 2-L shake flasks containing 400 mL rice bran or glucose – malt – yeast extract (GMY) – Mn-glycolate medium to produce MnP levels of 1.7 U·mL–1. These results show that the two strains of B. adusta, UAMH 7308 and 8258, can produce between two and three times the manganese peroxidase level of B. adusta BOS55, that they are good candidates for scale up of enzyme production, and that the rice bran medium supports higher levels of enzyme production than most previously described media.Key words: growth conditions, cereal bran, manganese peroxidase, Bjerkandera adusta, white rot fungi.


2015 ◽  
Vol 52 (2) ◽  
pp. 59-70 ◽  
Author(s):  
J. Vanags ◽  
L. Kunga ◽  
K. Dubencovs ◽  
V. Galvanauskas ◽  
O. Grīgs

Abstract Optimization of the microalgae cultivation process and of the bioprocess in general traditionally starts with cultivation experiments in flasks. Then the scale-up follows, when the process from flasks is transferred into a laboratory-scale bioreactor, in which further experiments are performed before developing the process in a pilot-scale reactor. This research was done in order to scale-up the process from a 0.4 1 shake flask to a 4.0 1 laboratory-scale stirred-tank photobioreactor for the cultivation of Desmodesmus (D.) communis microalgae. First, the effect of variation in temperature (21-29 ºC) and in light intensity (200-600 μmol m-2s-1) was studied in the shake-flask experiments. It was shown that the best results (the maximum biomass concentration of 2.72 g 1-1 with a specific growth rate of 0.65 g g-1d-1) can be achieved at the cultivation temperature and light intensity being 25 °C and 300 μmol m2s-1, respectively. At the same time, D. communis cultivation under the same conditions in stirred-tank photobioreactor resulted in average volumetric productivities of biomass due to the light limitation even when the light intensity was increased during the experiment (the maximum biomass productivity 0.25 g 1-1d-1; the maximum biomass concentration 1.78 g 1-1).


2020 ◽  
Vol 153 ◽  
pp. 865-874 ◽  
Author(s):  
S.T.L. Harrison ◽  
A. Kotsiopoulos ◽  
R. Stevenson ◽  
J.J. Cilliers
Keyword(s):  
Scale Up ◽  

2019 ◽  
Vol 91 (12) ◽  
pp. 1724-1746 ◽  
Author(s):  
Lutz Böhm ◽  
Lena Hohl ◽  
Chrysoula Bliatsiou ◽  
Matthias Kraume

2016 ◽  
Vol 7 (6) ◽  
pp. 1327-1337 ◽  
Author(s):  
Marcelo Adriano Corrêa Maceno ◽  
Luciana Porto de Souza Vandenberghe ◽  
Adenise Lorenci Woiciechowski ◽  
Carlos Ricardo Soccol ◽  
Michele Rigon Spier

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