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. 2017 Jul 24;10(6):1338–1352. doi: 10.1111/1751-7915.12776

Table 2.

Production of PHAs from food waste using recombinant bacteria

Food waste source Strain Plasmid PHA operon origin PHA polymer type Cultivation Dry cell Weight (g l−1) Maximum PHA Production Reported (g PHA g−1 dcw) References
Whey E. coli
GCSC657
pSYL107 C. necator PHB Shake flask 6.4 81% Lee et al. (1997)
Whey E. coli
GCSC657
pSYL107 C. necator PHB Fermenter, fed‐batch 87 80% Wong (1998)
Whey E. coli pSYL107 C. necator PHB Fermenter, fed‐batch 31 80% Kim (2000)
Whey E. coli
CML3‐1
pMAB26 C. necator PHB Fermenter, fed‐batch 33.09 28.65% Pais et al. (2014)
Whey E. coli
CGSC 4401
pJC4 Alcaligenes latus PHB Fermenter, fed‐batch 119.5 80.50% Ahn et al. (2000)
Whey E. coli
CGSC 4401
pJC4 Alcaligenes latus PHB Fermenter, fed‐batch 194 87% Ahn et al. (2001)
Whey E. coli pJC4 Alcaligenes latus PHB Fermenter, fed‐batch 14.5 71% Park et al. (2002)
Whey E. coli
K24K
pJP24K Azotobacter sp. FA8 PHB Fermenter, fed‐batch 70.1 72.90% Nikel et al. (2006)
Malt waste E. coli pUC19/PHA C. necator PHBV Fermenter, fed‐batch NA 16% Law et al. (2004)
Soy waste E. coli pUC19/PHA C. necator PHBV Fermenter, fed‐batch NA 23% Law et al. (2004)
Soy waste E. coli
XL1‐Blue
pKS C. necator PHB Fermenter, batch 3.025 27.83% Hong et al. (2000)
Organic acids E. coli
pnDTM2
NA NA PHB Fermenter, batch 2.9 45% Eshtaya et al. (2013)
Starch Aeromonas Sp. KC007‐R1 pRK415
H16
C. necator PHB Fermenter, batch 1.83 32.70% Chien and Ho (2008)

NA is not available.