Table 2 Influence of different nitrogen sources on dry biomass, GLA and lipid production parameters by coculture fermentation.

From: Coculturing of Mucor plumbeus and Bacillus subtilis bacterium as an efficient fermentation strategy to enhance fungal lipid and gamma-linolenic acid (GLA) production

Parameter

Organic nitrogen sources

In-organic nitrogen sources

Ammonium tartrate

Yeast extract

Malt extract

Peptone

Casein

Urea

Sodium nitrate

Ammonium chloride

Ammonium sulfate

Axenic fungus (control)*

Dry biomass (g/L)

10.5 ± 0.2

9.14 ± 0.1

9.12 ± 0.1

10.88 ± 0.2

9.66 ± 0.1

10.24 ± 0.1

8.93 ± 0.1

10.88 ± 0.2

12.95 ± 0.11

10.4 ± 0.22

Lipid yield (g/L)

2.83 ± 0.01

1.91 ± 0.01

2.69 ± 0.01

2.72 ± 0.01

2.51 ± 0.02

1.48 ± 0.01

2.50 ± 0.02

2.44 ± 0.01

3.62 ± 0.03

2.34 ± 0.04

Specific yield of lipid (Yp/x)

0.27 ± 0.0

0.21 ± 0.01

0.29 ± 0.0

0.25 ± 0.01

0.26 ± 0.02

0.14 ± 0.0

0.28 ± 0.02

0.22 ± 0.0

0.28 ± 0.02

0.22 ± 0.03

Lipid content (%)

27 ± 0.35

21 ± 0.18

29.5 ± 0.50

25 ± 0.22

26 ± 0.38

14.5 ± 0.10

28 ± 0.25

22.5 ± 0.35

28 ± 0.33

22.5 ± 1.30

GLA content (%, TFA)

13.7 ± 0.1

11.54 ± 0.3

11.53 ± 0.2

12.43 ± 0.3

11.89 ± 0.2

16.23 ± 0.2

11.15 ± 0.1

10.71 ± 0.1

13.39 ± 0.1

9.5 ± 0.1

Volumetric biomass production rate,Qx (g/L/d)

2.62 ± 0.01

2.28 ± 0.01

2.28 ± 0.01

2.72 ± 0.02

2.41 ± 0.01

2.56 ± 0.02

2.23 ± 0.02

2.72 ± 0.02

2.23 ± 0.01

2.6 ± 0.05

Volumetric lipid production rate (Qp)

0.70 ± 0.01

0.47 ± 0.0

0.67 ± 0.01

0.68 ± 0.02

0.62 ± 0.01

0.37 ± 0.0

0.62 ± 0.01

0.61 ± 0.01

0.90 ± 0.03

0.59 ± 0.02

  1. *Axenic fungus cultured on K&R medium containing glucose as a carbon source besides ammonium tartrate and yeast extract as nitrogen sources at pH 6.0 and 28 °C for 4 days.