Automatic bioprocess control. 1. A general concept.

Automation of bioprocesses is presented and discussed. A general concept is applied to laboratory scale reactors as well as to large scale production facilities consisting of many unit operations with a hierarchical and highly modular structure. The implementation of non-dedicated and intelligent analytical subsystems is foreseen. Hard- and software requirements are discussed in view of the functional requirements of both scientific research and production engineering. Some practical experience is reported using several different components in parallel installations.     

Production of cloned human leukocyte interferon by Bacillus subtilis: optimal production is connected with restrained growth.

Bacillus subtilis, transformed with a plasmid containing the human alpha-2 (leukocyte) interferon gene, was cultivated in batch and continuous culture in a complex medium. In continuous culture with dissolved oxygen of less than 10% of air saturation, the extracellular interferon titer decreased sharply when the growth rate was lower or higher than the optimal one (mu = 0.14 h-1). Thus, a relatively low growth rate was best for extracellular interferon production, and oxygen limitation enhanced interferon production. The mean output rate in batch culture after successful harvest was 20 X 10(6) IU/liter per h and the maximal output rate in continuous culture was 14 X 10(6) IU/liter per h.     

Changes in carbohydrate composition and trehalase-activity during the budding cycle of Saccharomyces cerevisiae

Summary The carbohydrate composition and the specific activity of the trehalase of cyclic partially synchronised yeast populations have been investigated. Under glucose limitation and appropriate cultural conditions synchronous growth in a chemostat was achieved. The cells accumulated the reserve carbohydrates during the single cell phase between two buddings. The rapid degradation of part of these reserves began shortly before the swelling of the bud. The importance of the mobilisation of endogenous reserves for the development of the cell is discussed.The specific activity of the trehalase changed during the budding cycle. The result gives rise to the assumption that the synthesis of this enzyme is linked to the growth cycle.     

Functional Expression of the Alkane-Inducible Monooxygenase System of the Yeast: Candida tropicalis IN Saccharomyces cerevisiae

The genes for the alkane-inducible monooxygenase system of the yeast Candida tropicalis, namely a cytochrome P450_alk (P450_alk) and a NADPH cytochrome P450 oxidoreductase (NCPR) gene, were transferred in Saccharomyces cerevisiae. The P450_alk gene was expressed in this host with the help of the yeast alcohol dehydrogenase I (ADHI) promoter and terminator, whereas the NCPR gene could be expressed with its own structural elements. The presence of P450_alk in S. cerevisiae microsomal fractions resulted in a new acquired lauric acid terminal hydroxylation activity. Moreover, the same activity, coupled with the appearance of 12-hydroxylauric acid derivatives, could be obtained by the addition of lauric acid to intact cells expressing P450_alk. The coordinate expression of the P450_alk and NCPR genes in S. cerevisiae elevated the turnover rate of the P450_alk monooxygenase activity about 2-fold.     

Pseudomonas aeruginosa biosurfactant production in continuous culture with glucose as carbon source

Rsan-ver, a strain of Pseudomonas aeruginosa isolated at this department, was used for the development of a continuous process for biosurfactant production. The active compounds were identified as rhamnolipids. A final medium for production was designed in continuous culture by means of medium shifts, since the formation of surface-active compounds was decisively influenced by the composition and concentration of the medium components. In the presence of yeast extract, biosurfactant production was poor. For the nitrogen-source nitrate, which was superior to ammonium, an optimum carbon-to-nitrogen ratio of ca. 18 existed. The iron concentration needed to be minimized to 27.5 micrograms of FeSO4 X 7H2O per g of glucose. A carbon-to-phosphate ratio below 16 yielded the maximum production of rhamnolipids. The final productivity dilution rate diagram indicated that biosurfactant production was correlated to low growth rates (dilution rate below 0.15 h-1). With a medium containing 18.2 g of glucose liter-1, a biosurfactant concentration (expressed as rhamnolipids) of up to 1.5 g liter-1 was obtained in the cell-free culture liquid.     

On-line measurements of culture fluorescence: Method and application

Summary In this paper a new probe allowing the measurement of NAD(P)H-dependent culture fluorescence in a bioreactor is presented. This sterilizable probe can be inserted in every bioreactor using a standard fitting of 25 mm. Under well defined conditions high specificity and sensitivity as well as high stability are further advantages of this probe. Application examples are given to demonstrate the operation possibilities of this fluorescence probe. In batch growth the culture fluorescence can be used for on-line estimation of biomass concentration. Metabolic alterations due to substrate of oxygen deficiency can easily be detected by fluorometric measurements. In kinetic studies the fluorescence probe is of great use because of a very small time delay.     

The production of cellulolytic enzymes by fungal cultures

Summary Twelve fungal cultures belonging to the genera ofAspergillus, Tricboderma, Chaetomium, Stachybotrys, andHypocrea were screened for the production of cellulolytic activity. All twelve were found to degrade xylan, avicel, and carboxymethylcellulose, More cellulolytic activity was obtained with shaken cultures than with still cultures and the addition of citrate-phosphate buffer to the media greatly depressed the levels of cellulolytic activity. Varying the composition of the mineral salts in the medium had no effect on the cellulolytic activity.The growth ofAspergillus wentii under controlled conditions in a bioreactor showed that the cellulolytic activity was not affected by the aeration rate or the type of stirrer. The rate of stirring, however, did effect the cellulolytic activity, as at lower stirring speeds considerable wall growth occurred which resulted in low levels of cellulolytic activity.Culture supernatant fromAspergillus wentii was found to hydrolyze from 30–32% of Solka-Floc and from 2–10% of corn cobs, wheat straw, and newsprint. The extensive hydrolysis of the Solka-Floc indicates that with suitably treated cellulosic wastes and appropriate enzymes, appreciable amounts of sugars could be obtained.