Citric acid was produced from glucose in repeated-batch shake-flask and continuous air-lift cultivations by calcium-alginate-immobilized Yarrowia lipolytica A-101 yeast. The medium composition was systematically studied in a batch system by using experimental design and empiric modelling. The highest citric acid product concentration of 39 g/1 was reached with a medium containing 150 g/1 of glucose, 0.105 g/1 of potassium dihydrogen phosphate, 0.84g/I of magnesium sulphate and 21 mg/1 of copper sulphate (5.2 rag/1 of copper). The results were further improved by hardening the alginate carrier beads with glutaraldehyde, and by activation of the immobilized biocatalyst in a nutrient solution. In continuous air-lift bioreactors with varying height-to-diameter ratio the highest productivity of 350 rag/1 per hour with a dilution rate of 0.023 1/h and a citric acid product concentration of 12 g/1 was reached with a ratio of 3.