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Table 4 Fermentation efficiency of A. succinogenes fed-batch cultures carried out using OFMSW hydrolysate

From: Evaluation of organic fractions of municipal solid waste as renewable feedstock for succinic acid production

Initial and consumed carbon sources (g/L)a

Nitrogen source (g/L)

MgCO3 (g/L)

Succinic acid (g/L)

Yield (g/g)a

Productivity (g/L/h)

By-product: succinic acid (g/g)

50 (57.9)

5 g/L CSL

5

28.7

0.50

0.41

0.37

50 (68.4)

5 g/L YE

5

34.3

0.50

0.75

0.59

50 (55.1)

5

31.1

0.56

0.62

0.30

50 (57.1)

10

31.7

0.56

0.72

0.25

50 (58.4)

20

34.8

0.60

0.79

0.25

  1. aConsumed carbon source is presented in the brackets; succinic acid to sugars conversion yield has been calculated based on quantity (g) of succinic acid produced during fermentation and the quantity (g) of total sugars added in the bioreactor