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Table 3 Preliminary evaluation of the change in medium cost and bioreactor capital cost associated to the switch from standard medium to agricultural byproduct-based medium

From: Effect of oxygen mass transfer rate on the production of 2,3-butanediol from glucose and agro-industrial byproducts by Bacillus licheniformis ATCC9789

Parameter

Units

Standard medium tests

Byproduct-based tests

Glucose concentration (kg/m3)

kg/m3

40

–

Beef extract concentration (kg/m3)

kg/m3

10

–

Soy peptone concentration (kg/m3)

kg/m3

10

–

Molasses concentration (kg/m3)

kg/m3

–

74

CMBM concentration (kg/m3)

kg/m3

–

30

BD/sugar yield (kg/kg)

kg/kg

0.44

0.235

BD productivity (kg/m3/day)

kg/m3/day

21.8

13.0

Total medium cost ($/m3)

$/m3

41

13

Reactor volume (m3)

m3

1.53

2.57

Medium cost ($/kgBD produced)

$/kgBD produced

2.33

1.20

Bioreactor capital cost ($/kgBD produced)

$/kgBD produced

0.10

0.16

Medium + bioreactor cost ($/kgBD produced)

$/kgBD produced

2.42

1.36