Skip to main content
. 2021 Mar 29;13(7):1084. doi: 10.3390/polym13071084

Figure 6.

Figure 6

PHA production using tung oil as a carbon source in batch fermentation. (a) biomass, polyhydroxyalkanoate (PHA) accumulation, (b) PHA monomer composition. 3HB, 3-hydroxybutyrate; 3HV, 3-hydroxyvalerate; DCW, dry cell weight; HHx, 3-hydroxyhexanoate.