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. 2021 May 14;13(10):1576. doi: 10.3390/polym13101576

Table 6.

Cell dry weight, PHA production, and monomer composition of PHA produced by A. vinelandii ΔAvin_16040 mutant strain, C. necator PHB4, and C. necator Re2058 transconjugants.

Strain 1 Concentrations of Na4HB (g/L) Cell Dry Weight (g/L) 2 PHA Content (%) 3 PHA Concentration (g/L) 4 Monomer Composition (mol.%)
3HB 4HB
A. vinelandii ΔAvin_16040 mutant strain 2 4.0 ± 0 e 54 ± 1 d 2.2 ± 0 e 90 ± 0 10 ± 0
4 3.5 ± 0 d 48 ± 0 c 1.7 ± 0 d 87 ± 0 13 ± 0
6 3.0 ± 0.1 c 42 ± 1 bc 1.3 ± 0 c 84 ± 0 16 ± 0
8 2.5 ± 0.1 b 36 ± 0 ab 0.9 ± 0 b 80 ± 0 20 ± 0
10 2.0 ± 0.1 a 34 ± 3 a 0.7 ± 0 a 78 ± 0 22 ± 0
No precursor 4.3 ± 0.1 f 55 ± 2 d 2.4 ± 0 f 100 ± 0 0
C. necator PHB4 containing phaC of A. vinelandii mutant cell 0.5 3.7 ± 0 a 40 ± 3 a 1.5 ± 0.1 a 95 ± 0 5 ± 0
1 3.8 ± 0 ab 43 ± 2 ab 1.6 ± 0.1 ab 94 ± 0 6 ± 0
1.5 4.0 ± 0 bc 46 ± 2 ab 1.8 ± 0.1 ab 93 ± 0 7 ± 0
2 4.0 ± 0 c 49 ± 3 b 2.0 ± 0.1 b 93 ± 0 7 ± 0
2.5 4.0 ± 0 bc 45 ± 1 ab 1.8 ± 0 ab 93 ± 0 7 ± 0
No precursor 4.9 ± 0.1 d 62 ± 2 c 3.0 ± 0.2 c 100 ± 0 0
C. necator Re2058 containing phaC of A. vinelandii mutant cell 0.5 4.3 ± 0.1 b 45 ± 2 a 2.0 ± 0.1 a 100 ± 0 0
1 4.6 ± 0 c 49 ± 0 b 2.3 ± 0 b 97 ± 0 3 ± 0
1.5 4.7 ± 0 cd 50 ± 1 b 2.3 ± 0.1 bc 97 ± 0 3 ± 0
2 4.8 ± 0 de 51 ± 0 b 2.5 ± 0 cd 96 ± 0 4 ± 0
2.5 5.0 ± 0 e 53 ± 1 b 2.6 ± 0.1 d 95 ± 0 5 ± 0
No precursor 4.0 ± 0 a 45 ± 1 a 1.8 ± 0 a 100 ± 0 0

Data shown are means of triplicate. The superscripts represent the significant difference of the data using statistical analysis (p < 0.05) for each bacterial strain. Superscript alphabets for each column that are different indicate a significant difference.1 A. vinelandii ΔAvin_16040 mutant strain and the transconjugants were cultivated using 30 g/L of fructose and 0.54 g/L of urea at 30 °C with agitation speed of 200 rpm. A. vinelandii ΔAvin_16040 mutant strain was cultivated for 72 h while the transconjugants were cultivated for 48 h. Different concentrations of Na4HB were used. ‘No precursor’ indicates no addition of precursor in the medium. 2 Cell dry weight was obtained after freeze-drying process. 3 PHA content of freeze-dried cell was determined using gas chromatography. 4 PHA concentration = cell dry weight * (PHA content/100).