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Aspergillus niger spores were used as catalyst in the bioconversion of glucose to gluconic acid. Spores produced by solid-state fermentation were treated with 15 different terpenes including monoterpenes and monoterpenoids to permeabilize and inhibit spore germination. It was found that spore membrane permeability is significantly increased by treatment with terpenoids when compared to monoterpenes. Best results were obtained with citral and isonovalal. Studies were carried out to optimize spores concentration (10(7)-10(10) spores/mL), terpene concentrations in the bioconversion medium and time of exposure (1-18 h) needed for permeabilization of spores. Fed-batch production of gluconate was done in a bioreactor with the best conditions [10(9) spores/mL of freeze-thawed spores treated with citral (3% v/v) for 5 h] followed by sequential additions of glucose powder and pH-regulated with a solution containing 2 mol/L of either NaOH or KOH. Bioconversion performance of the spore enzyme was compared with the commercial glucose oxidase at 50, 60, and 70 degrees C. Results showed that the spore enzyme was comparatively stable at 60 degrees C. It was also found that the spores could be reutilized for more than 14 cycles with almost similar reaction rate. Similar biocatalytic activity was rendered by spores even after its storage of 1 year at -20 degrees C. This study provided an experimental evidence of the significant catalytic role played by A. niger spore in bioconversion of glucose to gluconic acid with high yield and stability, giving protection to glucose oxidase.

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Aims:  To study the metabolic profile of Pseudomonas rhodesiae and Pseudomonas fluorescens in water–organic solvent systems using terpene substrates for both growth and biotransformation processes and to determine the aerobic or anaerobic status of these degradation pathways. Materials and Methods:  Substrates from pinene (α‐pinene, α‐pinene oxide, β‐pinene, β‐pinene oxide, turpentine) and limonene (limonene, limonene‐1,2‐oxide, orange peel oil) families were tested. For the bioconversion, the terpene‐grown biomass was concentrated and used either as whole cells or as a crude enzymatic extract. Conclusion:  Pseudomonas rhodesiae was the most suitable biocatalyst for the production of isonovalal from α‐pinene oxide and did not metabolize limonene. Pseudomonas fluorescens was a more versatile micro‐organism and metabolized limonene in two different ways. The first (anaerobic, cofactor‐independent, noninducible) allowed limonene elimination by synthesizing α‐terpineol. The second (aerobic, cofactor‐dependent) involved limonene‐1,2‐oxide as an intermediate for energy production through a β‐oxidation process. Significance and Impact of the Study:  Enzymatic isomerization of β‐ to α‐pinene was described for the first time for both strains. Alpha‐terpineol production by P. fluorescens was very efficient and appeared as a promising alternative for the commercial production of this bioflavour.

Optimization studies on the synthesis of isonovalal from alpha-pinene oxide by Pseudomonas rhodesiae CIP 107491 operated in a biphasic medium are presented. Three key parameters are identified. The first is the need for a permeabilization of cells by freezing them and then treating the thawed material with an organic solvent such as chloroform, toluene or diethyl ether. This operation allows both enzyme release into the aqueous phase outside the cells and an improvement in the transport properties of both substrate and product across the cell membrane, strongly increasing reaction rates. The second is that the enzyme alpha-pinene oxide lyase, which exhibits an irreversible inactivation by isonovalal (or a by-product), presents a constant turn-over, i.e., the total product synthesis is proportional to the biomass loading and is close to 108 mmol (16.4 g) isonovalal l(-1) g(-1) biomass. The third phenomenon is that the biphasic system used is not phase-transfer-limited, a feature attributed to the spontaneous formation of an oil-in-water emulsion. It is thus possible to carry out a very efficient process, allowing the recovery of 2.63 mol isonovalal l(-1) (400 g l(-1)) from 25 g biomass l(-1) in 2.5 h, corresponding to an average reaction rate as high as 0.70 mmol min(-1) g(-1) cells (160 g l(-1) h(-1)).

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