Skip to main content
. 2022 Apr 18;13(4):9645–9661. doi: 10.1080/21655979.2022.2057760

Table 2.

HA production under different fermentation conditions by Streptococci sp

Microorganism Fermentation
Mode (capacity)
Culture medium nutrients Fermentationparameters Biomass/ HA yield/MW References
S. equisubsp. zooepidemicus (ATCC 35246) Batch 2 L Marine by-products: Mussel processing wastewater (50 g L−1), tuna peptone (8 g L−1) 500 rpm
No aeration
3.67 g L−1/ 2.46 g L−1/ 2.5MDa [31]
S. zooepidemicus Batch bioreactor By-products: Sugarcane molasses and corn steep liquor 500 rpm
1 vvm
pH 6.7
3.48 g L−1/ 3.8MDa (Amado et al., 2017)
S. equisubsp. zooepidemicus (ATCC 35246) Batch 2.5 L Maltose (g L−1) increasing Carbon source consumed in CDM 600 rpm
1.3 vvm
2 g L−1/
2.14 g L−1/ 2.1 MDa
(Chong andNelsen, 2003)
Streptococcussp. Chemostatsbioreactor giving Continuousform Chemically defined medium (CDM) High dilution rate HA production 25% higher than batch cultures [32]
S. zooepidemicus G1 (mutant of ATCC 39920) Batch5L with strategy plus pulsed carbohydrate added Glucose (40 g L−1), polypeptone (20 g L−1), YE (10 g L−1) 10–80% DO 3.5 g L−1/ 2.19MDa [33]
S. zooepidemicus WSH 24 Fed-batch 7 L Sucrose (70 g L−1), YE (25 g L−1) 200 rpm
0.5 vvm
16.3 g L−1/ 6.6 g L−1/ n.d. (Liu et al., 2009)
S. equisubspzooepidemicus (ATCC 39920) Batch 10 L Sucrose (50 g L−1), casein hydrolysate (10 g L−1) 400 rpm
2 vvm
6.5 g L−1/ 5.1 g L−1/ 3.9 MDa [34]
Streptococcus sp. ID9102 (KCTC 1139BP) Batch 75 L Glucose (4%), YE (0.75%), casein peptone (1%), Gln+Glu+ oxalic acid 400rpm 0.5 vvm 3 g L−1/ 6.94 g L−1/ 5.9 MDa (Imet al., 2009)
S. zooepidemicus (ATCC 39920) Batch 3 L Glucose (20 g L−1), YE (10 g L−1 + acetoin and acetate 300 rpm
1 vvm
2.43 g L−1/ 2.15 g L−1/ n.d. Wuet al., 2009
S. equisubspzooepidemicus (ATCC 35246) Batch 2 L Glucose (60 g L−1), CDM 600 rpm
1 vvm
3.5 g L−1/ 4.2 g L−1/ 3.2MDa [35]

CDM: Chemically defined medium. NTG: N-methyl-N’-nitro-N-nitrosoguanidin. phbCAB genes: polyhydroxybutyratesynthesis genes. YE: yeast extract