Additional file 4. Depiction of ammonium concentrations in the culture medium and reservoir of the multi-component fed-batch cultivations at varied initial glucose concentrations and 40 g/L ammonium carbonate in the reservoir. Depiction of (a) Oxygen transfer rate; (b) Ammonium concentration in the culture medium; (c) Ammonium concentration in the reservoir; Cultivation conditions: Wilms-MOPS-mineral medium (culture medium: 200 mM MOPS with 7 g/L initial ammonium sulfate, initial reservoir glucose concentrations: 250/375/500/750 g/L, 40 g/L ammonium carbonate, blue dextran concentration: 1 g/L), temperature: 37 °C, shaking frequency: 350 rpm, shaking diameter: 50 mm, initial culture medium volume: 10 mL, inoculation OD600: 0.5, reservoir fi...
Additional file 4. Influence of maximum oxygen transfer capacities on acetoin formation with Bacillu...
Additional file 3. Cultivation parameters of eight E. coli BL21(DE3) clones grown under inducing con...
Additional file 2: Table S2. Performance parameter for individual pulses of pulsed fed-batch cultiva...
Additional file 5. Depiction of cultivations with 750 g/L glucose and 40 g/L ammonium carbonate in t...
Additional file 3. Comparison of calculated and measured values at varied initial reservoir glucose ...
Additional file 8. Effect of dipotassium phosphate concentration variation on OTR in cultivations wi...
Additional file 7. Uncorrected and corrected cell dry weight results for multicomponent fed-batch cu...
Additional file 9. Average values and standard deviations for validation of reproducibility. Depicti...
Additional file 2. Effect of membrane thickness of a dialysis membrane on oxygen transfer rate in E....
Abstract Background Screening in the fed-batch operation mode is essential for biological cultivatio...
Additional file 1. Set-up of the membrane-based fed-batch shake flask. (a) The offline and (b) The o...
Additional file 1. Reduced acidification during the cultivation of Bacillus licheniformis DSM 8785. ...
Additional file 2: Figure S2. Culture of E. coli BL21 pRhotHi YFP under oxygen-limited conditions in...
Additional file 2. Glucose consumption and product formation during different cultivations of Bacill...
Abstract Background The initial part of process development involves extensive screening programs to...
Additional file 4. Influence of maximum oxygen transfer capacities on acetoin formation with Bacillu...
Additional file 3. Cultivation parameters of eight E. coli BL21(DE3) clones grown under inducing con...
Additional file 2: Table S2. Performance parameter for individual pulses of pulsed fed-batch cultiva...
Additional file 5. Depiction of cultivations with 750 g/L glucose and 40 g/L ammonium carbonate in t...
Additional file 3. Comparison of calculated and measured values at varied initial reservoir glucose ...
Additional file 8. Effect of dipotassium phosphate concentration variation on OTR in cultivations wi...
Additional file 7. Uncorrected and corrected cell dry weight results for multicomponent fed-batch cu...
Additional file 9. Average values and standard deviations for validation of reproducibility. Depicti...
Additional file 2. Effect of membrane thickness of a dialysis membrane on oxygen transfer rate in E....
Abstract Background Screening in the fed-batch operation mode is essential for biological cultivatio...
Additional file 1. Set-up of the membrane-based fed-batch shake flask. (a) The offline and (b) The o...
Additional file 1. Reduced acidification during the cultivation of Bacillus licheniformis DSM 8785. ...
Additional file 2: Figure S2. Culture of E. coli BL21 pRhotHi YFP under oxygen-limited conditions in...
Additional file 2. Glucose consumption and product formation during different cultivations of Bacill...
Abstract Background The initial part of process development involves extensive screening programs to...
Additional file 4. Influence of maximum oxygen transfer capacities on acetoin formation with Bacillu...
Additional file 3. Cultivation parameters of eight E. coli BL21(DE3) clones grown under inducing con...
Additional file 2: Table S2. Performance parameter for individual pulses of pulsed fed-batch cultiva...