Ml. Wei et al., METABOLIC ENGINEERING OF SERRATIA-MARCESCENS WITH THE BACTERIAL HEMOGLOBIN GENE - ALTERATIONS IN FERMENTATION PATHWAYS, Biotechnology and bioengineering, 59(5), 1998, pp. 640-646
Serratia marcescens was transformed with plasmid vector pUC8 or pUC8 c
ontaining the bacterial (Vitreoscilla) hemoglobin gene (vgb) on either
a 2.3-kb fragment (pUC8:15) or 1.4-kb fragment (pUC8:16) of Vitreosci
lla DNA. The vgb-bearing strains were compared with the pUC8 transform
ant and untransformed S. marcescens with respect to growth in Luria-Be
rtani (LB) broth supplemented with glucose or casein acid hydrolysate.
Growth (on a viable cell basis) was similar to that in unsupplemented
LB. Total acid excretion (as estimated by medium pH) was similar for
all strains in both LB plus 2% casein acid hydrolysate and LB without
additions. Acid excretion in LB plus 2% glucose was somewhat greater a
t up to 10 h in culture for the two vgb-bearing strains; from 10 to 26
h in culture, the pHs of these cultures continued to decrease (to 4.1
-4.2), whereas those of the non-vgb-bearing strains returned to near t
he starting pH (7.4-7.8). Concomitantly, after 26 h of culture in LB p
lus 2% glucose, the non-vgb-bearing strains had produced about 15 time
s as much acetoin and about three to four times as much 2,3-butanediol
as the vgb-bearing strains. In general, for all strains, much more ac
etoin and 2,3-butanediol were produced in LB plus 2% glucose than in u
nsupplemented LB. The exception was acetoin production by the strain b
earing vgb on plasmid pUC8:15; after 26 h of culture in LB without sup
plementation it was between three and four times that of the other str
ains, and about 50% higher than its level in LB plus 2% glucose. When
grown with the 2% casein acid hydrolysate supplement, the strain beari
ng vgb on plasmid pUC8:15 produced much more acetoin and 2,3-butanedio
l than the other strains after 26 hours in culture. The results confir
m that vgb can significantly alter carbon metabolism and suggest that
the use of vgb technology for directed metabolic engineering may be a
complicated process, depending in part on medium composition. (C) 1998
John Wiley & Sons, Inc. Biotechnol Bioeng 59: 640-646,1998.