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. 2017 Apr 20;101(14):5603–5614. doi: 10.1007/s00253-017-8281-x

Table 1.

Overview over cultivations—process variables and outcomes

FB ID q s gluc
(g/(g × h))
q s ara
(g/(g × h))
q s total
(g/(g × h))
x ara
(%)
μ
(1/h)
Titer
(g/l)
k
(−)
LE
(%)
Purity hom.
(%)
Purity lysed
(%)
1 0.220 0.055 0.275 20.0 0.08 3.2 70
2 0.240 0.059 0.299 19.8 0.10 2.5 −.54 81.9 61 53
3 0.263 0.143 0.406 35.1 0.12 2.1 −1.25 99.0 50 47
4 0.202 0.222 0.423 52.3 0.16 1.5 −.52 90.2 55 41
5 0.119 0.051 0.179 28.4 0.05 4.0 −.74 75.5 58 55
6 0.127 0.127 0.254 50.0 0.09 3.5 −.47 61.7 61 54
7 0.131 0.141 0.272 51.9 0.10 3.8 −.7 47.4 57 60
8 0.135 0.227 0.362 62.7 0.12 2.5 −.92 75.6 49 43
9 0.080 0.087 0.168 52.1 0.05 6.1 −.97 39.3 71 59
10 0.049 0.152 0.200 75.8 0.07 5.3 −0.68 31.0 79 58

The cultivations are numbered with a fed-batch ID (FB ID). Values for the mean q s D-glucose (q s gluc), q s L-arabinose (q s ara), q s total, and specific growth rate (μ) during the induction phase are given. Furthermore, the L-arabinose concentration in the mixed feed (x ara) is shown. The rhBMP-2 titer at the end of the induction phase (titer) represents the productivity in each process. Information about E-lysis can be taken from the maximal lysis efficiency (LE) and the lysis reaction coefficient k. The purity is presented for homogenized samples at the end of the induction phase (purity hom.) and an E-lysed non-homogenized sample at maximal E-lysis efficiency (purity lysed)