For the complete utilization of maltodextrin, the reaction was performed in a one-pot, two-step mode. When 100 mM IA-debranched maltodextrin was used as the substrate, the first step was initiated under the abovementioned conditions at optimized enzyme concentrations predicted by Model 2 (displayed in Supplementary Table
Engineered Pathway for Maltodextrin-to-PHB Conversion
For the complete utilization of maltodextrin, the reaction was performed in a one-pot, two-step mode. When 100 mM IA-debranched maltodextrin was used as the substrate, the first step was initiated under the abovementioned conditions at optimized enzyme concentrations predicted by Model 2 (displayed in Supplementary Table
Corresponding Organization :
Other organizations : Tianjin Institute of Industrial Biotechnology, Chinese Academy of Sciences
Variable analysis
- Temperature (37 °C)
- Enzyme concentrations (PhaA at 0.78 mU/mL, other enzymes at 1 U/mL, PhaC at 20 U/mL)
- Maltodextrin concentration (100 mM, 200 mM)
- Substrate addition strategy (one-pot, one-step; one-pot, two-step; fed-batch)
- Production of PHB
- Maltodextrin utilization
- Optical density (OD600) of the reaction mixture
- Buffer composition (200 mM Tris-HCl, pH 7.4)
- Cofactor concentrations (10 mM MgCl2, 0.5 mM MnCl2, 0.5 mM TPP, 0.5 mM CoA, 2 mM NADP+)
- Antibiotics (10 μg/mL ampicillin, 5 μg/mL kanamycin)
- Sodium phosphate (10 mM, pH 7.4)
- Positive control: Not explicitly mentioned.
- Negative control: Not explicitly mentioned.
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