Effect of CO partial pressure on cell-recycled continuous CO fermentation by Eubacterium limosum KIST612

Authors
Chang, ISKim, BHLovitt, RWBang, JS
Issue Date
2001-12-10
Publisher
ELSEVIER SCI LTD
Citation
PROCESS BIOCHEMISTRY, v.37, no.4, pp.411 - 421
Abstract
Eubacterium limosum KIST612 was cultivated on carbon monoxide using a cell-recycled continuous fermentation system to produce organic acids. A bubble column reactor system (k(L)a = 72 h(-1)) was used with a membrane to allow on-line products removal with cell recycle. When cell concentration reached 5.25 g l(-1) in the reactor, the cell concentration did not increase at carbon monoxide (CO) partial pressures lower than 74 kPa though CO was consumed with the acidic products formation. At this stage, the overall CO mass transfer rate (k(L)a[C* - C-L]) was lower than required for the maximum cell growth (q(CO)(X)(max) but higher than that to meet the maintenance requirement (m(s)X). When the CO mass transfer rate was maintained higher than maintenance requirement by increasing CO partial pressure, the cell concentration increased to 9.5 g l(-1). (C) 2001 Elsevier Science Ltd. All rights reserved.
Keywords
SYNTHESIS GAS; CARBON-MONOXIDE; MAINTENANCE ENERGY; GROWTH; BIOCONVERSION; SYNTHESIS GAS; CARBON-MONOXIDE; MAINTENANCE ENERGY; GROWTH; BIOCONVERSION; acetogen; Eubacterium limosum; carbon monoxide; synthesis-gas; mass transfer limitation; organic acid
ISSN
1359-5113
URI
https://pubs.kist.re.kr/handle/201004/139916
DOI
10.1016/S0032-9592(01)00227-8
Appears in Collections:
KIST Article > 2001
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