Scale translation from shaken to diffused bubble aerated systems for lycopene production by Blakeslea trispora under stimulated conditions.

This study deals with the scale up of Blakeslea trispora culture from the successful surface-aerated shake flasks to dispersed-bubble aerated column reactor for lycopene production in the presence of lycopene cyclase inhibitor 2-methyl imidazole. Controlling the initial volumetric oxygen mass transfer coefficient (kLa) via airflow rate contributes to increasing cell mass and lycopene accumulation. Inhibitor effectiveness seems to decrease in conditions of high cell mass. Optimization of crude soybean oil (CSO), airflow rate, and 2-methyl imidazole was arranged according to central composite statistical design. The optimized levels of factors were 110.5 g/L, 2.3 vvm, and 29.5 mg/L, respectively. At this optimum setting, maximum lycopene yield (256 mg/L) was comparable or even higher to those reported in shake flasks and stirred tank reactor. 2-Methyl imidazole use at levels significantly lower than those reported for other inhibitors in the literature was successful in terms of process selectivity. CSO provides economic benefits to the process through its ability to stimulate lycopene synthesis, as an inexpensive carbon source and oxygen vector at the same time.

Accuracy of computer-assisted implant placement with insertion templates.

OBJECTIVES: The purpose of this study was to assess the accuracy of computer-assisted implant insertion based on computed tomography and template-guided implant placement. MATERIAL AND METHODS: A total of 246 implants were placed with the aid of 3D-based transfer templates in 181 consecutive partially edentulous patients. Five groups were formed on the basis of different implant systems, surgical protocols and guide sleeves. After virtual implant planning with the CoDiagnostiX Software, surgical guides were fabricated in a dental laboratory. After implant insertion, the actual implant position was registered intraoperatively and transferred to a model cast. Deviations between the preoperative plan and postoperative implant position were measured in a follow-up computed tomography of the patient's model casts and image fusion with the preoperative computed tomography. RESULTS: The median deviation between preoperative plan and postoperative implant position was 1.0 mm at the implant shoulder and 1.4 mm at the implant apex. The median angular deviation was 3.6º. There were significantly smaller angular deviations (P=0.000) and significantly lower deviations at the apex (P=0.008) in implants placed for a single-tooth restoration than in those placed at a free-end dental arch. The location of the implant, whether in the upper or lower jaw, did not significantly affect deviations. Increasing implant length had a significant negative influence on deviations from the planned implant position. There was only one significant difference between two out of the five implant systems used. CONCLUSION: The data of this clinical study demonstrate the accuracy and predictable implant placement when using laboratory-fabricated surgical guides based on computed tomography.

Formulated squalene for food related applications.

Squalene (SQ), the sterol precursor in all cell types, is a functional lipid of high importance, as currently an array of benefits to human health are recognized. It has chemopreventive and photooxidative properties, it protects human from coronary heart diseases and is also used to maintain skin health. Technological properties of SQ have been widely appreciated in fields beyond human consumption. Moreover, SQ forms stable nanoemulsions and, as found in several conformations, it forms SQ-drug conjugates with improved properties and potentially can be used as an important bioactive ingredient carrier. As far as food applications are concerned, its thermal stability and contribution in the stability of frying oils are well established. All of the above properties increased both food and non-food SQ applications so that its current demand in food, pharmaceuticals and cosmeceuticals is getting higher. Sharks, the richest SQ source, are endangered species. Consequently, the need for search of new SQ sources, mainly of plant origin, is increased. Biotechnology gives also some interesting alternatives. In this review article, the most recent patents regarding SQ extraction, production as well as its food-related applications are presented. Squalane, the hydrogenated counterpart of squalene, is also discussed.

Recovery of squalene from wine lees using ultrasound assisted extraction-a feasibility study.

The present work is a systematic approach for valorization of wine lees regarding the recovery of squalene, a bioactive lipid. Such a study is presented for the first time in literature. Separate examination of squalene content in "light" and "heavy" lees from different vinification processes by RP-HPLC demonstrated that these waste streams can be used as a source for this lipid, despite variations due to technological or genetic effects. Next, ultrasound assisted extraction of squalene from the "industrial waste" (the mixture of wine lees generated from different wines) using n-hexane was optimized with the aid of response surface methodology (independent variables: sonication duration and duty cycles). Autolysis was monitored through optical microscopy. Squalene yield (0.6 ± 0.08 g SQ/kg dry lees) was comparable to that of recently examined potential sources (0.2-0.35 g SQ/kg dry olive pomace and 0.06 g SQ/kg olive leaves).

Enhanced squalene production by wild-type Saccharomyces cerevisiae strains using safe chemical means.

Interest is increasing in establishing renewable sources for squalene, a functional lipid, as the conventional ones are limited. In the present study, squalene production was achieved in a wild-type laboratory Saccharomyces cerevisiae strain by two safe chemical means using terbinafine (0.05-0.55 mM) and methyl jasmonate (MJ) (0-1.00 mM). Bioprocess kinetics optimized by response surface methodology and monitored by high-performance liquid chromatography revealed a clear dependence of growth and squalene content (SQC) and yield (SQY) on the above regulators. Maximum SQC (10.02±0.53 mg/g dry biomass) and SQY (20.70±1.00 mg/L) were achieved using 0.442 mM terbinafine plus 0.044 mM MJ after 28 h and 0.300 mM terbinafine after 30 h, respectively. A 10-fold increase in SQY was achieved in comparison to that in the absence of regulator. The ruggedness of optimum conditions for SQY was verified for five industrial strains. The cellular lipid fraction (∼12% of dry biomass) was rich in squalene (12-13%). Results are encouraging toward bioprocess scale up.

Squalene versus ergosterol formation using Saccharomyces cerevisiae: combined effect of oxygen supply, inoculum size, and fermentation time on yield and selectivity of the bioprocess.

The dynamics of two wild type strains of Saccharomyces cerevisiae (BY4741 and EGY48) that vary in the ability to produce sterols were compared in batch cultures under different aeration conditions. Poor supply of oxygen enhanced selectivity of the bioprocess in favor of squalene formation. Optimization of inoculum size and fermentation time arranged according to a central composite statistical design revealed significant differences between the strains in terms of yield and productivity. Experimental verification showed that an optimized bioprocess under semianaerobic conditions is competitive with regard to those reported in the literature. Maximum squalene yield and productivity were, respectively, 2967.6 +/- 118.7 microg/L of culture medium and 104 +/- 4.2 microg/Lh for BY4741 and 3129 +/- 109.5 microg/L of culture medium and 155.9 +/- 5.5 microg/Lh for EGY48. The prospect of developing high-purity squalene preparations that meet food safety regulation demands is expected to attract the interest of the food industry.

Industrial glycerol as a supplementary carbon source in the production of beta-carotene by Blakeslea trispora.

The dynamics of industrial types of glycerol as a supplementary carbon source to glucose for beta-carotene production by Blakeslea trispora was investigated in batch cultures. The growth kinetics, cellular lipid accumulation-degradation, substrate assimilation, and beta-carotene production were clearly dependent on the level of addition of pure glycerol. The highest beta-carotene production (15.0 mg/g of dry biomass) was obtained at an initial glycerol concentration of 60.0 g/L. Substitution of pure glycerol by the nonpurified soap byproduct did not inhibit cell growth. Conversely, partial purification of the biodiesel byproduct by removing methanol and fatty acids was unavoidable for cell growth. Both types of industrial glycerol stimulated beta-carotene synthesis more than 10 (soap byproduct) and 8 times (biodiesel byproduct) compared to control medium. The maximum beta-carotene contents were 10 and 8 mg/g of dry biomass, respectively, and its relative content in the carotenoid fraction was 86-88%.