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. 2020 Dec 10;8(12):1959. doi: 10.3390/microorganisms8121959

Table 2.

Recombinant rhamnolipid production in batch experiments in this study compared to other Pseudomonas producers.

Organism Medium Substrate (conc. in g/L) Duration Maximal RL Titer (g/L) Growth Condition Ref.
P. putida
KT42C1 pVLT31_rhlAB
LB Glucose (10) 42 h 1.5 Flask, aerobic [11]
P. putida
KT2440 pSynPro8
LB Glucose (10) 22 h 3.22 Flask, aerobic [10]
P. putida KT2440 * pSynPro8oT ModR Glucose (253) 72 h 14.9 Benchtop bioreactor, aerobic [38]
P. putida KT2440 Δflag SK4 Delft Glucose (11) 10 h 1.48 Benchtop bioreactor, aerobic [16]
P. putida RL KT2440 pJNN.rhlAB LB Glucose (10) 30 h 0.73 Microscale, aerobic this study
P. putida RL KT2440 pJNN.rhlAB Delft Glucose (10) 30 h
72 h
0.36
0.11
Microscale, aerobic
Flask, aerobic
this study
P. putida RL-PCA
KT2440 pJNN.rhlAB_pBNT.14phz2
Delft Glucose (10) 30 h
72 h
0.11
0.15
Microscale, aerobic
Flask, aerobic
this study
P. putida RL-PCA KT2440 pJNN.rhlAB_pBNT.14phz2 Delft Glucose (5) 10 d 0.02 Benchtop BES, PA ** this study
P. putida RL-PCA KT2440 pJNN.rhlAB_ pBNT.14phz2 Delft Glucose (5) 25 d 0.03 Electrobioreactor BES, PA ** this study

* Data in this row represent the highest titer achieved with recombinant P. putida. However, this process was operated in fed-batch with a continuous glucose feed and does not allow for direct comparison with other presented data from batch operations. ** PA: passive aeration via open vent filters.