Analysis of the calcium-dependent interaction of calmodulin with bovine serum albumin

An air-driven ultracentrifuge has been used to investigate the calcium-dependent association between calmodulin and bovine serum albumin. Procedures were described which allowed the interaction to be analyzed to yield the equilibrium constant. At low ionic strength (25 mm Tris-HCl, pH 7.5, pCa 6.68, 9°C) the equilibrium constant for the interaction was estimated to be 2.1 × 10⁴m⁻¹, while at high ionic strength (25 mm Tris-HCl, pH 7.5, 150 mm KCl, pCa 6.68, 9°C) the value was 4.5 × 10³m⁻¹. Under similar conditions, calmodulin was also found to interact with β-lactoglobulin A and gelatin, but no detectable association was observed with ovalbumin.     

The role of carbon dioxide in glucose metabolism of Bacteroides fragilis

The effect of CO₂ concentration on growth and glucose fermentation of Bacteroides fragilis was studied in a defined mineral medium. Batch culture experiments were done in closed tubes containing CO₂ concentrations ranging from 10% to 100% (with appropriate amounts of bicarbonate added to maintain the pH at 6.7). These experiments revealed that CO₂ had no influence on growth rate or cell yield when the CO₂ concentration was above 30% CO₂ (minimum available CO₂–HCO ₃ ^- , 25.5 mM), whereas a slight decrease in these parameters was observed at 20% and 10% CO₂ (available CO₂–HCO ₃ ^- , 17 and 8.5 mM, respectively). If CO₂–HCO ₃ ^- concentrations were below 10 mM, the lag phase lengthened and a decrease in maximal growth rate and cell yield were observed. The amount of acetate made decreased, while d-lactate concentration increased. A net production of CO₂ allowed growth under conditions of extremely low concentrations of added CO₂.When B. fragilis was grown in continuous culture with 100% CO₂ or 100% N₂, the dilution rate influenced the concentrations of acetate, succinate, propionate, d-lactate, l-malate and formate formed. Decreasing the dilution rate favored propionate and acetate production under both conditions. When the organism was grown with 100% N₂, the amount of propionate formed was greater than the amount of succinate formed at all dilution rates. Except at slow dilution rates the reverse was true when 100% CO₂ was used. B. fragilis was unable to grow at dilution rates faster than 0.154 h^-1 when grown with 100% N₂; the Y _glc ^max was 67.9 g DW cells/mol glucose and m _s was 0.064 mmol glucose/g DW·h. If the gas atmosphere was 100% CO₂ the organism was washed out of the culture when the dilution rate exceeded 0.38 h^-1; the Y _glc ^max was 59.4 g DW cells/mol glucose and m _s was 0.094 mmol glucose/g DW·h.Measurement of the phosphoenolpyruvate (PEP) carboxykinase (E.C. 4.1.1.49) with whole, permeabilized cells of B. fragilis showed an increase of specific enzyme activity with decreasing CO₂ concentrations. The mechanisms used by B. fragilis to adjust to low levels of CO₂ are discussed.     

Culture method to study fungal growth in solid fermentation

Summary A new culture method is described to study the growth of Aspergillus niger on cassava meal in the solid state. This method uses preparations of the cooked starchy substrate as a homogeneous granulated product containing spores, salts and water. An incubation device aerates the mass with humidified air at a controlled temperature. Homogeneous development of mycelia, without sporulation, occurred in the substrate mass. From physiological studies, optimal conditions for A. niger growth on cassava in the solid state were 50–55% moisture, 35°C, a nitrogen source comprising 60% ammonium and 40% urea (on a nitrogen basis) and 2×10⁷ spores/g of substrate. Growth kinetics were established and changes in pH, protein, carbohydrate and water content were determined during the incubation. Growth rate and yield were quite similar to those described in the literature for A. niger cultivated in liquid media under optimal conditions.     

Use of the 82Sr/82Rb Generator in Clinical PET Studies

The use of the ⁸²Sr/⁸²Rb generator in clinical positron emission tomography (PET) studies of myocardial perfusion has been described. An infusion pump is used to deliver the short-lived ⁸²Rb from the generator to the patient. Various characteristics of the generator and the infusion system are described. The ⁸²Rb yield was 69.8 ± 13.3% and the ⁸²Sr breakthrough was always less than the limit of 0.02 μCi/mCi ⁸²Rb. The yield of ⁸²Rb increased with the flow rate and the potency of the generator. Patients with coronary artery disease were studied for myocardial perfusion abnormalities by the ⁸²Rb PET technique and images of excellent diagnostic quality were obtained.     

Environmental conditions during glycerol bioconversion affect 3-hydroxypropionic acid bioproduction by Limosilactobacillus reuteri DSM 17938

3-Hydroxypropionic acid (3-HP) is a platform molecule whose biological production was carried out by the bacterium Limosilactobacillus reuteri according to a two-step process: first, a growth phase in batch mode on glucose, then a glycerol bioconversion into 3-HP in fed-batch mode. With the objective of improving 3-HP bioproduction, this study aimed at defining the operating conditions during the bioconversion phase that increases the bioproduction performance. A central composite rotatable design allowed testing various pH levels and specific glycerol feeding rates. By establishing response surfaces, optimal conditions have been identified that were different depending on the considered output variable (final 3-HP quantity, 3-HP production yield and production rate). Of them, 3-HP final quantity and 3-HP production yield were maximized at pH 6.0 and at specific glycerol feeding rates of 60 and 55 mg_gly g_CDW⁻¹ h⁻¹, respectively. The specific 3-HP production rate was the highest at the upper limit of the specific substrate feeding rate (80 mg_gly g_CDW⁻¹ h⁻¹) but was not affected by the pH. An additional experiment was carried out at pH 6.0 and a specific glycerol feeding rate of 80 mg_gly g_CDW⁻¹ h⁻¹ to validate the previous observations. In conclusion, the results showed a significant improvement of 3-HP concentration by 13%, of specific production rate by 34% and of 3-HP volumetric productivity by 39%, as compared to the initial values.     

Spore Yield and Microcycle Conidiation of Colletotrichum gloeosporioides in Liquid Culture

The effect of V8 juice concentration (5 to 40%, vol/vol), spore inoculum density (10⁵ and 10⁷ spores per ml), and liquid batch or fed-batch culture condition on mycelium and spore production by Colletotrichum gloeosporioides was evaluated. The amount of mycelium produced, the time required for initiation of sporulation following attainment of maximum mycelium, and the time for attainment of maximum spore concentration increased with increasing V8 juice concentration in batch culture. Cultures containing V8 juice at >10% achieved a similar spore density (apparent spore-carrying capacity) of about 0.8 mg of spores per ml (1 × 10⁷ to 2 × 10⁷ spores per ml) independent of inoculum density and V8 juice concentration. The relative spore yield decreased from a high of 64% of the total biomass for the low-inoculum 5% V8 culture, through 13% for the analogous 40% V8 culture, to a low of 2% for the high-inoculum 27% V8 culture. Fed-batch cultures were used to establish conditions of high spore density and low substrate availability but high substrate flux. The rate of addition of V8 juice was adjusted to approximate the rate of substrate utilization by the (increasing) biomass. The final spore concentration was about four times higher (3.0 mg of spores per ml) than the apparent spore-carrying capacity in batch culture. This high spore yield was obtained at the expense of greatly reduced mycelium, resulting in a high relative spore yield (62% of the total biomass). Microcycle conidiation occurred in the fed-batch but not batch systems. These data indicate that substrate-limited, fed-batch culture can be used to increase the amount and efficiency of spore production by C. gloeosporioides by maintaining microcycle conidiation conditions favoring allocation of nutrients to spore rather than mycelium production.     

Microbial transformations of steroids

The preparation ofΔ ^{1, 4} , 17-dione fromΔ ⁴ , 17-dione with the aid ofFusarium lateritium 403 is described, the yield being 80%, referred to the original steroid. The undesirable 1-dehydrotestololactone is formed under the given conditions only in traces. If progesterone was used as the starting steroid the yield of the undesirable 1-dehydrotestololactone is 40%, referred to the progesterone used. Dehydroepiandrosterone was not transformed by theFusarium lateritium strain to steroid metabolites. During the preparation of 1-dehydrotestosterone fromΔ ⁴ -androstene-3, 17-dione, using two successive microbial procedures (dehydrogenation of the A ring in position 1–2 and reduction of the keto group at C₁₇ giving rise to the corresponding 17β-hydroxy derivative), the isolation yield was 55–60%, referred to the starting steroid.     

Enzymatic production of l-tryptophan from dl-5-indolylmethylhydantoin by Flavobacterium sp.

An enzymatic production of l-tryptophan from dl-5-indolylmethylhydantoin by the action of hydantoinase and carbamoylase has been investigated. A strain identified as (Flavobacterium) sp. I-3 isolated from soil was found to form l-tryptophan from dl-5-indolylmethylhydantoin. Cultural conditions for the formation of the l-tryptophan-forming activity were investigated, and the highest activity of 0.81 μmol min⁻¹of l-tryptophan formed per 1 ml of culture broth (hydantoinase, 3.6 μmol min⁻¹of N-carbamoyl-l-tryptophan formed per 1 ml of culture broth; carbamoylase, 0.92 μmol min⁻¹of l-tryptophan formed per 1 ml of culture broth) was obtained. These activities were found to be inducible and intracellular. Optimization of the parameters of the conversion reaction resulted in accumulation of 50 mg of l-tryptophan per 1 ml of cultural broth per day. The conversion yield from dl-5-indolylmethylhydantoin was about 100%. Accumulated l-tryptophan was readily isolated in pure form by ordinary procedures.     

Protein synthetic ability of Escherichia coli valine transfer RNA with pseudouridine, ribothymidine, and other uridine-derived residues replaced by 5-fluorouridine

The requirement for pseudouridine and other uridine-derived minor nucleotides for activity of transfer RNA in several of the intermediate steps in protein synthesis was examined using a purified preparation of Escherichia coli valine transfer RNA in which the uridine and uridine-derived nucleotides were replaced by 5-fluorouridine. The degree of substitution was 87% or better for uridine, pseudouridine, ribothymidine, dihydrouridine, and 4-thiouridine, and at least 75% for uridine-5-oxyacetic acid. Each of these nucleotides, except for uridine, occurs only once in this transfer RNA species.The rate and yield of ternary complex formation with elongation factor Tu-GTP of E. coli, the rate and extent of elongation factor-dependent binding to ribosomes at 10 mm-Mg²⁺, and the rate and extent of synthesis of the co-polypeptide (Phe_n,Val) dependent on poly(U₃,G) were all unchanged when the fluorouridine-containing transfer RNA was used in place of the normal control. In all yield assays, the amount of product formed was proportional to the amount of valyl-tRNA added. Non-enzymatic binding to ribosomes in the presence of tetracycline was more efficient for the fluorouridine-substituted tRNA than for the control. At 15 to 20 mm-Mg²⁺ the polynucleotide-dependent binding, as a percentage of tRNA added, was 44% for the control and 65% for the modified tRNA, while at 5 mm-Mg²⁺, the figures were 10% and 40%, respectively.We conclude from these results that there is no essential requirement for pseudouridine or ribothymidine in the GTψC loop of tRNA for its proper functioning in protein synthesis in vitro. Confirming earlier work, dihydrouridine and 4-thiouridine are also not essential.     

Design of acidogenic reactors for the anaerobic treatment of the organic fraction of solid food waste

Volatile Fatty Acids (VFA) production by anaerobic fermentation of organic solid wastes was studied at laboratory scale. The influence of initial substrate concentration was evaluated on VFA production. Completely mixed reactors (0.9?l) were used at mesophilic temperature (35?°C). Food wastes had 43.8% Total Solids content. Three dilutions of substrate (1/25, 1/10 and 1/5) corresponding to 1.75%, 4.38% and 8.76% of Total Solids and five values of Organic Loading Rates: 2, 5, 10, 12.5 and 25?kg COD/m³?d were studied. It was found that substrate 1/10 led to 14?g VFA/l at a loading rate of 12.5?kg COD/m³?d and an hydraulic retention time of 3.7 d. The main VFA produced were especially acetate and butyrate. Substrate diluted 1/5 led to 26.1?g VFA/l at a loading of 5?kg COD/m³?d and an hydraulic retention time of 15.1 d, but biomass production was not optimal. In a second study, a cascade of three reactors was used. An effluent with 42?g VFA/l was obtained at steady-state conditions at a loading of 12.5?kg of COD/m³?d and an hydraulic retention time of 12.5?d. The distribution of VFA was the following: 36% of propionate, 34% of acetate and 22.5% of butyrate.     

Inoculation of pea by application of Rhizobium in the planting furrow

Summary Selected streptomycin resistant strains ofRhizobium leguminosarum suspended in nutrient broth were added to the planting furrow immediately before the sowing of pea. The nodule occupancy by a strain isolated from Risø soil (Risø la) was increased from 74 to 90%, when the inoculum rate was increased from 3.7×10⁶ to 3.7×10⁸ cells per cm row. The experimental soil contained 10³ to 10⁴ cells ofR. leguminosarum per gram. An almost inefficient strain isolated from Risø soil (SV10) was less competitive with respect to nodulation on two pea cultivars than an efficient Risø strain (SV15) and an efficient non-Risø strain (R1045). The nodule occupancy by the introduced strains varied between pea cultivars.Irrespective of the generally high nodulation by the efficient strains introduced to the soil, the pea seed yield, compared to pea nodulated by the indigenous population, was not significantly increased. Neither were two commercial inoculants, applied in rates corresponding to 3 times the recommended rate, able to increase the yield. This suggests that the indigenous populations ofR. leguminosarum were sufficient in number and nitrogen fixing capacity to ensure an optimal pea crop. However, some inoculation treatments slightly increased the seed N concentration and total N accumulation, indicating that it may be possible to select or develop bacterial strains that may increase the yield.     

Ethanol fermentation characteristics of Thermoanaerobacter ethanolicus

Thermoanaerobacter ethanolicus is an extreme thermophilic non-spore forming ethanol-producing anaerobic bacterium. Minimum nutrient requirements and optimum growth conditions have been established. An optimum yeast extract-glucose ratio for ethanol yield has also been determined. Initial medium pH, optimally 7.5–8.0, significantly affected the amount of ethanol formed. Maximum specific growth rate was found to be 0.22 h^?1at pH 7.5 and 69°C. Ethanol concentration up to 11 g l^?1at pH 7.5 and 69°C was used to characterize ethanol inhibition. The growth kinetics of T. ethanolicus were characterized in terms of environmental parameters. Substrate utilization, ethanol formation and inhibition by both sugar and ethanol were also quantified.     

Hydrolysis of crambe oil by enzymatic catalysis: An evaluation of the operational conditions

Abstract

In this work, the enzymatic hydrolysis of the crambe oil by using a commercial immobilized lipase Lipozyme RM IM was evaluated. The effect of the operational conditions, such as temperature, water/oil molar ratio, enzyme/substrate mass ratio and stirring speed were assessed based on the experimental designs. The experiments were performed in a closed and batch system with controlled temperature and stirring speed. In addition, the kinetics of the process was studied in the best operational conditions, wherein the experimental data were obtained and described by a mathematical model. The influence of the operational conditions was assessed based on the measured values of the free fatty acids (FFA) produced by the enzymatic hydrolysis. In 4?h of reaction, a yield of 42.6% was observed and the most significant operational conditions were the enzyme/substrate mass ratio and stirring speed. By the kinetic investigation, an initial reaction rate of 3.5?×?10⁴?mol?mL^?1?h^?1 and a maximum yield of 74% were observed after 40?h of reaction (in the equilibrium condition). The mathematical model was not only able to adequately describe the experimental data of FFA concentrations profiles but also showed predictive capacity to independents assays in different operational conditions. Therefore, based on the simulation analysis of the enzymatic hydrolysis of the crambe oil, the model can be useful for process optimization and phenomenological studies.     

Exogenous salicylic acid stimulates physiological and biochemical changes to improve growth, yield and active constituents of fennel essential oil

Fennel (Foeniculum vulgare Mill) is a high-value medicinal and essential oil bearing plant used extensively in pharmaceutical, food and cosmetic industries. A pot experiment was carried out in the natural conditions of net house to resolve whether the foliar application of salicylic acid (SA) might enhance the growth, yield and essential oil production of fennel. Plants were sprayed three times with SA. The first spray was carried out at 40?days after sowing (DAS); the second and third sprays were applied one and 2?weeks later, the plants were sprayed with deionised water (control) and different concentrations of SA (10^?5, 10^?4 and 10^?3?M). The foliar spray of SA at 10^?4?M significantly enhanced the vegetative growth (shoot and root lengths, fresh and dry weights), physiological and biochemical characteristics (chl ??a??, chl ??b??, total chlorophyll and carotenoids contents, nitrate reductase activity, carbonic anhydrase activity, leaf-N, -P and -K contents), yield characteristics (number of umbels and fruits, 1,000-seed weight and seed yield) and essential oil yield of fennel. GLC analysis revealed the significant increase in the components of essential oil, viz. trans-anethole (80.4?C84.7?%), methyl chavicol (2.3?C2.5?%) and fenchone (5.6?C7.9?%). It was concluded that foliar spray of SA at 10^?4?M might be employed for enhancing the plant growth as well as yield and quality of essential oil of fennel.     

Production of raw-starch-hydrolysing α-amylase from the newly isolated Geobacillus thermodenitrificans HRO10

An extracellular raw-starch-digesting α-amylase was isolated from Geobacillus thermodenitrificans HRO10. The culture conditions for the production of α-amylase by G. thermodenitrificans HRO10 was optimized in 1.2–l bioreactor using full 2⁴ and 3² factorial designs. From the optimal reaction conditions, a model (Y = − 594.206 − 0.178T² − 8.448pH² + 6.020TpH − 0.005T²pH²) was predicted, which was then used for α-amylase production. In the bioreactor studies, the enzyme yield under optimized conditions (pH 7.1, 49°C) was 30.20 U/ml, a 51% improvement over the results (19.97 U/ml) obtained when the traditional one-factor-at-a-time method was employed. This α-amylase does not require extraneous calcium ions for activity, which may be a commercially important observation.     

Transforming growth factor-β in the early mouse embryo: Implications for the regulation of muscle formation and implantation

In a search for functions of transforming growth factor-β during early embryonic development we used two different experimental approaches. In the first we made use of embryonic stem (ES) cells. ES cells in culture differentiate to derivatives of all three germ layers and mimic some aspects of organogenesis when grown as aggregates in suspension to form embryoid bodies. Differentiation procedes further when the embryold bodies attach to suitable substrates. Muscle and neuronal cells are among the most readily identified cell types then formed. We examined the effect of all-trans retinoic acid (RA) and members of the transforming growth factor-β family(TGF-βl, TGF-β2) under these conditions in an assay where single aggregates formed in hanging microdrops in medium supplemented with serum depleted of lipophilic substances which would include retinoids. Endoderm-like cells formed under all conditions tested. RA at concentrations of 10⁸ M and 10⁷ M induced the formation of neurons but in the absence of RA or at concentrations up to 10?⁹ M, neurons were not observed. Instead, beating muscle formed in about one-third of the plated aggregates; this was greatly reduced when RA concentrations increased above 10?⁹ M. Immunofluorescent staining for muscle specific myosin showed that two muscle cell types could be distinguished: elongated, non-contractile myoblasts and mononucleate flat cells. The mononucleate flat cells appeared to correspond with rhythmically contracting muscle. The number of non-contractile myoblasts increased 3-fold over controls in the presence of 10?⁹ M RA. TGF-βs increased the number of contractile and non-contractile muscle cells by a factor 3 to 7 over controls, depending on the TGF-β isoform added and the muscle cell type formed. TGF-β2 also invariably increased the rate at which contracting muscle cells were first observed in replated aggregates. The stimulatory effect of TGF-βs on the formation of mononucleate flat cells was completely abrogated by RA at 10?⁹ M while the number of myoblasts under similar conditions was unchanged. These data suggest that a complex interplay between retinoids and TGF-β isoforms may be involved in regulation of differentiation in early myogenesis. In the second approach, neutralizing polyclonal rabbit antibodies specific for TGF-β2 were injected into the cavity of mouse blastocysts 3.5 days post coitum (pc). After 1 day in culture, embryos were transferred to pseudopregnant females. The number of decidua, embryos and resorptions were counted at day 8.5–9.5 pc. Control antibody injected embryos implanted with high efficiency (87%) compared with anti-TGF-β2 injected embryos which implanted with an efficiency of only 43%. If empty decidua (resorptions) were included, the overall recovery was 71% and 32% for control and experimental embryos, respectively. Embryos that were recovered showed no overt macroscopic abnormalities. These results together impiy functions for TGF-βs in implantation as well as in later development of the embryo. © 1993Wiley-Liss, Inc.     

The production of bacteriophage μ2

In three series of experiments, 3-l., 20-l., and 150-l. bacterial cultures were grown in stirred, deep culture vessels to average bacterial cell densities of 71 × 10⁸, 63 × 10⁸, and 43 × 10⁸ viable organisms per milliliter, respectively, and then infected with phage. The average yield of progeny phage in each case was ca. 3000 mpfu (minimum plaque-forming units) per cell. Thus, the average mass of phage obtained in the 3-l. experiments was not less than 124 mg./l., calculated from the plaque counts, assuming a particle size of 3.6 × 10⁶ Daltons for the μ2 phage. This is about twentyfold higher than is obtainable by conventional methods in aerated, shaken culture flasks. The actual phage yields are probably much higher than the minimum values calculated from plaque counts. For example, in the case of one of our culture lysates which was purified at King's College, the efficiency of plating was shown to be only 19%. The carbon dioxide evolution rate of cultures was measured and used as a guide to the time at which phage should be added. In this way, greater control of cultural conditions was obtained than is possible in shaken flasks. For the best yield of phage per milliliter of culture, the optimum time for phage infection was such that bacterial lysis just prevented the carbon dioxide evolution rate from reaching its potential maximum. The major factor influencing the phage yield per milliliter of culture was the aeration capacity of the culture vessel used. All had maximum aeration capacities much higher than those obtainable in shaken culture flasks. Cultures grown and infected in 3-l. Vessel operated under conditions of low aeration gave poor yields of phage. The reason for this are discussed.     

Extraction of lipids and pigments of Chlorella vulgaris by supercritical carbon dioxide: influence of bead milling on extraction performance

The influence of bead milling on the extraction of lipids and pigments by supercritical carbon dioxide was investigated in this study. Different operating parameters for the 3-h process were first tested on raw Chlorella vulgaris; 600 bar was the optimum pressure at 60 °C with a carbon dioxide flow rate of 30 g min^?1. Under these operating conditions, 10 % of total lipid containing chlorophyll and carotenoids with 1.61 and 1.72 mg g^?1 dry weight of microalga, respectively, has been recovered. Microscopic observation was used to assess a cell wall breakage through bead milling, which produced positive results in terms of increasing the yield of biomolecules of interest. Thus, under the same operating conditions, the yield of total lipid extract, chlorophyll and carotenoids increased significantly. Moreover, the addition of a polar co-solvent to a raw microalga had a considerable effect on the final extract. Overall, the addition of 5 % w v^?1 ethanol to a raw microalga increased the total extract yield by 27 %, and bead milling increased the total extract yield by 16 %. Chlorophyll and carotenoids were also significantly affected by the addition of ethanol, with an 81 and 65 % increase with a raw microalga and a 61 and 52 % increase using bead milling, respectively.     

Metabolism of progesterone in mouse vaginal tissue

The $\text{in vitro}$ and $\text{in vivo}$ metabolism of 1,2- ³H-progesterone was studied in estrogen-stimulated and control vaginae of ovariectomized mice. Employing two-dimensional thin-layer chromatography, gas-liquid chromatography and metabolite “trapping” techniques, the major and minor pathways for progesterone metabolism were determined $\text{in vitro}$ and shown to involve saturation of the Δ⁴-double bond to yield 5α-pregnane compounds and reduction of the C20 and C3 ketone groups to form 20α- and 3α- and 3β-hydroxy derivatives, respectively. The quantities of 20β-hydroxy metabolites and 5β-epimers that were detected were considered not to be significant. The major metabolites formed by untreated tissues following $\text{in vitro}$ incubation in the presence of both high (10^?6M) and low (10^?8M) progesterone concentrations were 3α-hydroxy-5α-pregnan-20-one and 5α-pregnane-3,20-dione. Although these two derivatives were also found in sizable quantities in estrogen-treated tissues, a marked increase (5-fold) in the rate of C20 ketone reduction at high progesterone concentrations (10^?6M) to yield 20α-hydroxy-4-pregnen-3-one was demonstrated. Following intravaginal administration of ³H-progesterone $\text{in vivo}$, only progesterone and 3α-hydroxy-5α-pregnan-20-one were retained in appreciable quantities through 2 hr, suggesting rapid loss of 20α-hydroxy-4-pregnen-3-one and the 5α-pregnanediols from this tissue under $\text{in vivo}$ conditions.     

An Improved Synthesis of 1-β-D-Arabinofuranosylcytosine 5′-Phosphate-L-1,2-diacylglycerols

Abstract

5′-O-MMTr-cytosine arabinoside was prepared on a large scale from 5′-O-MMTr-cytidine with diphenyl carbonate via 5′-protected cytidine-2′,3′-carbonate-aracytidine-2′,2-anhydro derivative at a 67 % yield. The synthesis of 1,2-L-dipalmitoyl-snglycerol, 1,2-L-distearoyl-sn-glycerol and 1,2-L-dioleoyl-sn-glycerol described here using 9-fluorenylmethoxycarbonyl (FMOC) group for protection of 3-position of glycerol which can be selectively removed by Et₃N treatment on the overall 60–70 % yield based on 1.2,-isopropilidene-sn-glycerol. These glycerols were phosphorylated first with 2-chlorophenyl-phosphoro-bis-triazolide quantitatively¹ in order to avoid acyl migration, then the glycerophosphate intermediates were condensed with 2′,3′,N⁴-trileulinyl-l-β-D-arabinofuranosylcytosine in the presence of 2-mesytilenesulphonyl chloride (MsCl) and 1 -methylimidazole (Melm)-which was used in the coupling of nucleotides²-^? in an 85–95 % yield compared with the low yielding diester method of Ryu³. Deblocking was carried out in two steps with tetrabutylammonium fluoride (TBAF) and hydrazine hydrate, producing target compouns (14a, 14b, 14c) at a 50 % yield.