Table 6 |
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|
A comparison of 2,3-butanediol productivity in a packed bed biofilm reactor with productivities in other reactor types |
||||
|
Reactor Type |
Culture |
Substrate |
Productivity [gL-1h-1] |
Reference |
|
|
||||
|
Biofilm, continuous |
K. pneumoniae |
Whey permeate |
11.70 |
[23] |
|
Batch (control) |
A. aerogenes |
Glucose |
1.10 |
[96] |
|
Continuous reactor (free cells) |
K. pneumoniae |
Glucose |
4.25 |
[97] |
|
Immobilized cell continuous |
K. pneumoniae |
Whey permeate |
2.30 |
[98] |
|
Cell recycle, continuous |
B. polymyxa |
Whey permeate |
1.04 |
[95] |
|
Cell recycle, continuous |
K. pneumoniae |
Glucose |
9.84 |
[99] |
|
Cell recycle, continuous |
E. aerogenes |
Glucose |
5.40 |
[100] |
|
|
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|
Qureshi et al. Microbial Cell Factories 2005 4:24 doi:10.1186/1475-2859-4-24 |
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