The growth rate and the maximum cell concentration of methanotrophic b
acteria are limited by the transfer of methane and oxygen to the cultu
re fluid. The operation under moderate pressure results in an increase
in driving force for the mass transfer of both nutrients and, therefo
re, in a large increase in the attainable biomass concentration. Our l
aboratory pressure fermenter with a volume of 12 litres operates under
a system pressure of up to 0.5 MPa. In this reactor a maximum product
ivity of 6 g biomass/lh is achieved. However, operating under moderate
system pressure and exhaust gas recycling has also disadvantages beca
use the concentrations of the gas phase components may inhibit the gro
wth process. From the results of the laboratory fermenter we have deve
loped kinetic models of the influence of dissolved oxygen and carbon d
ioxide on the specific growth rate of the methanotrophic strain GB 25.
These models are the basis for processing under increased system pres
sure and exhaust gas recycling.