Erratum to: Anoxic metabolism and biochemical production in Pseudomonas putida F1 driven by a bioelectrochemical system

Table 2 Key process parameters of anaerobic glucose conversion of P. putida F1 in the anode compartment of a BES using [Co(bipy)₃]^3+/2+ or [Fe(CN)₆]^3−/4− as electron acceptors while poising the anode at +0.697 V vs SHE

	[Co(bipy)₃]^3+/2+	[Fe(CN)₆]^3−/4−
Carbon balance (%)	99.6	97.6
Coulombic efficiency (%)	98.5	93.3
Yields (mol_product/mol_glucose)
Y _2KGA	0.90 ± 0.03	0.90 ± 0.02
Y _{acetic acid}	0.073 ± 0.008	0.144 ± 0.012
Y _{gluconic acid}	0.31 ± 0.06	0.09 ± 0.03
	0.25 ± 0.03	0.09 ± 0.04
Y _electrons	3.94 ± 0.11	3.88 ± 0.07
Rates (mmol/(gCDW h))
r _glucose	−0.26 ± 0.04	−0.35 ± 0.07
r _{acetic acid}	0.019 ± 0.003	0.051 ± 0.010
r _2KGA	0.23 ± 0.04	0.32 ± 0.06
r _{gluconic acid}	0.08 ± 0.02	0.03 ± 0.01
	−0.06 ± 0.01	−0.03 ± 0.02
r _electrons	1.02 ± 0.18	1.37 ± 0.26

Data are fitted with linear regression using datasets from ten ([Fe(CN)₆]^3−/4−) and four ([Co(bipy)₃]^3+/2+) biological replicates with a total of 79 and 36 samples, respectively (compare Additional file 1: Fig. S3). Carbon balance is calculated from the fitted rates considering carbon content of molecules and assuming equimolar CO₂ production when making acetate from glucose. Gluconic acid is a product in the first 100 h and serves as a substrate thereafter, hence 2 yields and rates are given

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