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. 2015 Sep 4;14:127. doi: 10.1186/s12934-015-0312-7

Table 1.

Ethylene glycol production with different engineered E. coli strains expressing the synthetic pathway

Experimental conditions Final conc. (g/L) Yielda (mol/mol) (g/g) Productivity [g/(l h)] References
Xylonate pathway expressed in E. coli ΔxylA mutant [9]
 Shake flask (MM + 4 g/L xylose + 1 g/L peptone + 0.5 g/L yeast extract) 0.92 0.55 0.23 ni
 Bioreactor (MM + 40 g/L xylose + 10 g/L peptone + 5 g/L yeast extract, batch process) 11.7 0.71 0.29 0.24
(D)-ribulose-1P pathway (dte + fucA + fucO + fucK) expressed in E. coli ΔxylB ΔaldA (ΔendA ΔrecA) mutant [10]
 Shake flask (MM + 10 g/L xylose) 3.5 0.84 0.35 ni
 Bioreactor (MM + unknown amount of xylose, fed-batch process) 42.0 ni ni 0.6
(d)-xylulose-1P pathway (khkC + aldoB) expressed in E. coli ΔxylB mutant [8]
 Shake flask (MM + 10 g/L xylose) 1.9 0.45 0.19 ni
(d)-xylulose-1P pathway (khkC + aldoB + fucO) expressed in E. coli ΔxylB ΔaldA mutant This study
 Shake flask (MM + 10 g/L xylose) 4.1 0.94 0.39 ni
 Bioreactor (MM + 55 g/L xylose + 1 g/L peptone, batch process) 20.3 0.91 0.38 0.37

MM mineral salt medium, ni not informed.

aAll pathways listed in this table have a theoretical maximum EG yield on xylose of 0.41 g/g (1 mol/mol).