The keratin-degrading actinomycete Srrepromyces fradiae was cultured in a bioreactor of novel design in which the wool substrate was wound over a supporting frame partially immersed in salts medium and slowly rotated during the course of fermentation. Both disulphide reductase and keratinase enzyme activities were detected in culture supematants and the substrate was almost totally solubilized.

Streptomyces cattleya, S. fradiae and S. griseus produced different amounts of growth when cultured sequentially through sporulation, vegetative and antibiotic production media. Only S. griseus grew well on all three types of medium. Streptomyces cattleya grew poorly on both sporulation and vegetative media. Growth was 1.6 and 8.0 mg/1/h respectively. For all three species, biomass yield in the final antibiotic production medium was dependent on amount of inoculum. Antibiotic yields were obtained only from production media. Under slow growth conditions L-cysteine and L-valine supplementation stimulated S. cattleya beta-lactam production, giving 1000 micrograms/ml beta-lactam equivalents compared with 45 micrograms/ml beta-lactam equivalents for no supplementation. For aminoglycosides the agar well diffusion bioassay was more sensitive towards the hydrochloride than the neutral salt. Paper chromatography confirmed the main antibiotic classes. RF values for replicate samples indicated aminoglycoside homogeneity and beta-lactam heterogeneity.

Oil residues arising from the Christos-Bitas spillage were found to contain 28% of oil extractable by carbon tetrachloride; the remainder comprised water and undefined solids. When incubated in 8-L rectangular tanks with a mixed population of mainly bacteria to which diammonium hydrogen phosphate was added, ca. 97% of the Christos-Bitas oil fraction was degraded. When the same substrate was degraded by only three isolated Pseudomonas strains in 1-L cylindrical tanks, degradation was only ca. 56%. Raising the temperature from 20 to 50 degrees C brought about a visible loss in cell viability with only ca. 38% of the substrate degraded. Oil degradation proceeded in direct proportion to increases in cell attachment to the dispersed oil. The aliphatic fraction of Kuwait crude oil up to nC(25) measured by gas liquid chromatography (GLC) was oxidized within 48 h. Using this substrate the three pseudomonads together brought about a more complete degradation (87%) than a single Bacillus isolate. The Bacillusstrain was capable of deggrading between 50 and 65% of the crude, depending on whether diammonium hydrogen phosphate supplemented a peptone-based medium. The preferential biodgradability of fractions was the following aliphatics > aromatics > asphalts, as has been widely reported.

Oil residues arising from the Christos-Bitas spillage were found to contain 28% of oil extractable by carbon tetrachloride; the remainder consisted of water and undefined solids. Christos-Bitas mousse was added to 1.18 m(3) liquor inoculated with oil-contaminated marine mud, and aerated with a 1.5-hp vortex pump and venturi nozzle (12.5 mm) in a cylindrical tank. After 70 days, oil degradation reached 7 mg oil/L/h. About 98% of the solvent extractable oil added was degraded over 83 days. Analysis of oil residues harvested at the end of this experiment showed that there was a decreasing trend in percent degradation in the following order: aromatics > saturates > heterocyclics > asphalts. No less than 94% of any fraction analysed was degraded.In the second pilot trial, oil degradation was carried out in a cylindrical jacket tank containing 6.82 m(3) liquor inoculated with oil-contaminated marine mud from Penarth, South Wales, UK, together with pure cultures derived from the same source, and aerated with a 7.5-hp vortex pump and venturi nozzle (18 mm diameter). Mixing of the oil was inhomogeneous for the first 100-110 days. The overall degree of substrate dispersion and total oil balance was determined by sampling at different depths. Degradation by the mixed culture was achieved at the rate of 164 mg oil/L/h. After 224 days, this was equivalent to 9.6 x 10(3)/kg(-1)/yr;(214 kg/wk) for 6.82 m(3) of liquor. The degradation rate continued to rise as the feed rate was increased by means of an automatic, timed pump. A lag phase of five to six months was necessary to allow the mixed population to build up to an exploitable level.

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