2007
DOI: 10.1016/j.bej.2006.09.019
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Effects of post-induction feed strategies on secretory production of recombinant streptokinase in Escherichia coli

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Cited by 40 publications
(23 citation statements)
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“…On the other hand, there are few reports that demonstrate the absence of any correlation between these two factors [6][7][8]. Some authors have claimed that rather than the preinduction l, it is a high postinduction l, which helps in achieving high-level production of recombinant protein [9], whereas others have shown that the postinduction l is an intrinsic property of the cell that cannot be controlled by bioprocess strategies [10,11]. However, one problem associated with some of these reports is that they have looked at overall expression levels rather than the specific product formation rate (q p ), which is a better measure of product formation kinetics.…”
Section: Introductionmentioning
confidence: 91%
“…On the other hand, there are few reports that demonstrate the absence of any correlation between these two factors [6][7][8]. Some authors have claimed that rather than the preinduction l, it is a high postinduction l, which helps in achieving high-level production of recombinant protein [9], whereas others have shown that the postinduction l is an intrinsic property of the cell that cannot be controlled by bioprocess strategies [10,11]. However, one problem associated with some of these reports is that they have looked at overall expression levels rather than the specific product formation rate (q p ), which is a better measure of product formation kinetics.…”
Section: Introductionmentioning
confidence: 91%
“…Extensive work has been carried out on recombinant streptokinase expression in the E. coli host with upto 25,000 IU/mL of the recombinant protein. 38 The secretion of glycosylated streptokinase has been reported in P. pastoris (3200 IU/mL) with an improved proteolytic resistance and stability. 35 Recently, 4.25 g/L of bioactive streptokinase was produced in P. pastoris with a volumetric productivity of 3727 IU/mL/h.…”
Section: First Generation Plasminogen Activatorsmentioning
confidence: 99%
“…After the exhaustion of glucose, fed-batch experiments were performed by feeding the solutions containing glucose (100 g/l), yeast extract (100 g/l) and ampicillin 100 mg/l. Concentration of glucose in the medium was monitored at regular interval of time and fed by intermittent pulse feeding in proportional to the cell mass [17]- [19]. Feeding of glucose with specific feed rate of 0.5 g glucose per g DCW/h and 0.25 g glucose per g DCW/h was carried out in the growth phase and production phase, respectively and the residual glucose was maintained below 1.0 g/l [19] [20].…”
Section: Fed-batch Cultivationmentioning
confidence: 99%
“…Concentration of glucose in the medium was monitored at regular interval of time and fed by intermittent pulse feeding in proportional to the cell mass [17]- [19]. Feeding of glucose with specific feed rate of 0.5 g glucose per g DCW/h and 0.25 g glucose per g DCW/h was carried out in the growth phase and production phase, respectively and the residual glucose was maintained below 1.0 g/l [19] [20]. The biomass concentration in the bioreactor was calculated throughout the fermentation, by measuring the optical density (OD) as well as the dry cell weight.…”
Section: Fed-batch Cultivationmentioning
confidence: 99%