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Table 2 Parameters used for FA example

From: Evaluation of gas supply configurations for microbial product formation involving multiple gaseous substrates

Parameter

Value

Source

\(k_{L,\text{O}_2}a\)

6.0·10−2 s−1

(van ’t Riet and Tramper 1991)

\(C_{{{\text{O}}_{2} }}\)

6.0·10−2 mol/m3

(Fu et al. 2010)

\(C_{{{\text{CO}}_{2} }}\)

1.6 mol/m3

(Roa Engel et al. 2011)

\(D_{{{\text{O}}_{2} }}\)

2.1·10−9 m2/s

(Cussler 2009)

\(D_{{{\text{CO}}_{2} }}\)

1.9·10−9 m2/s

(Cussler 2009)

q p

5.3·10−2 kgP/(kgX·h)

(Roa Engel et al. 2011)

c X

50 kgX/m3

(Chang et al. 2014)

\(H_{{{\text{O}}_{2} }}\)

5.11·109 Pa

(Lide 2009)

\(H_{{{\text{CO}}_{2} }}\)

2.11·108 Pa

(Lide 2009)

V mol

1.81·10−5 m3/mol

Calculated

\(\rho_{{{\text{H}}_{2} {\text{O}}}}\)

9.94·102 kg/m3

(Lide 2009)

\(P_{{{\text{O}}_{2} }}\)

0.02–0.08 \(\$ / {\text{kg}}_{{{\text{O}}_{2} }}\)

(Sho Kobayashi and Hassel 2005)

\(P_{{{\text{CO}}_{2} }}\)

0.02–0.08 \(\$ / {\text{kg}}_{{{\text{CO}}_{2} }}\)

(Initiative 2012)

P Glc

0.68 $/kgGlc

(United States Department of Agriculture 2014)

P W

0.094 $/kWh

(Steelonthenet.com 2014)