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1.
Bioprocess Biosyst Eng ; 37(11): 2361-70, 2014 Nov.
Article in English | MEDLINE | ID: mdl-24861314

ABSTRACT

Cultivation of microorganisms in batch experiments is fast and economical but the conditions therein change constantly, rendering quantitative data interpretation difficult. By using chemostat with controlled environmental conditions the physiological state of microorganisms is fixed; however, the unavoidable stabilization phase makes continuous methods resource consuming. Material can be spared by using micro scale devices, which however have limited analysis and process control capabilities. Described herein are a method and a system combining the high throughput of batch with the controlled environment of continuous cultivations. Microorganisms were prepared in one bioreactor followed by culture distribution into a network of bioreactors and continuation of independent steady state experiments therein. Accelerostat cultivation with statistical analysis of growth parameters demonstrated non-compromised physiological state following distribution, thus the method effectively multiplied steady state culture of microorganisms. The theoretical efficiency of the system was evaluated in inhibitory compound analysis using repeated chemostat to chemostat transfers.


Subject(s)
Bioreactors/microbiology , Biomass , Equipment Design , Escherichia coli K12/growth & development , Escherichia coli K12/metabolism , Industrial Microbiology , Systems Biology
2.
J Biotechnol ; 145(1): 60-5, 2010 Jan 01.
Article in English | MEDLINE | ID: mdl-19861135

ABSTRACT

Specific growth rate dependent gene expression changes of Escherichia coli K12 MG1655 were studied by microarray and real-time PCR analyses. The bacteria were cultivated on glucose limited minimal medium using the accelerostat method (A-stat) where starting from steady state conditions (chemostat culture) dilution rate is constantly increased. At specific growth rate (mu) 0.47h(-1), E. coli had focused its metabolism to glucose utilization by down-regulation of alternative substrate transporters expression compared to mu=0.3h(-1). It was found that acetic acid accumulation began at mu=0.34+/-0.01h(-1) and two acetate synthesis pathways - phosphotransacetylase-acetate kinase (pta-ackA) and pyruvate oxidase (poxB) - contributed to the synthesis at the beginning of overflow metabolism, i.e. onset of acetate excretion. On the other hand, poxB, pta and ackA expression patterns suggest that pyruvate oxidase may be the only enzyme synthesizing acetate at mu=0.47h(-1). Loss of glucose and acetate co-utilization represented by down-regulation of acs-yjcH-actP operon between specific growth rates 0.3-0.42h(-1) and acetic acid accumulation from mu=0.34+/-0.01h(-1) allows one to surmise that the acetate utilization operon expression might play an important role in overflow metabolism.


Subject(s)
Escherichia coli K12/physiology , Gene Expression Profiling/methods , Oligonucleotide Array Sequence Analysis/methods , Acetates/metabolism , Cell Culture Techniques/methods , Culture Media , Energy Metabolism , Escherichia coli K12/genetics , Escherichia coli K12/growth & development , Escherichia coli K12/metabolism , Glucose/metabolism , Reproducibility of Results
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