Computer-aided control of water activity for lipase-catalyzed esterification in solvent-free systems

A computer system for on-line monitoring and control of the water activity (a(w)) in solvent-free media has been developed. The performance of this system was investigated by carrying out the lipase-catalyzed esterification of n-capric acid with n-decyl alcohol. A humidity sensor measured the relative humidity in the reactor headspace, which was then transmitted electrically to a digital computer that was used as a feedback controller. The water activity control was achieved by sparging either humidified air or dried air through the reaction medium at a flow rate determined by the digital feedback controller. The use of humid air and dry air for a(w) control made it possible to induce a larger a(w) gradient and thereby higher water transfer rate. As a result, the water activity quickly reached the desired a(w) values. We tested whether water activity in the reaction medium can be monitored by measuring relative humidity in the headspace. When the water activity in the liquid phase was determined from measurements of water content in the medium and compared to that measured directly with the humidity sensor, the a(w) in the reaction medium did not differ significantly from that in the headspace. This indicates that there is a near-equilibrium between the liquid medium and the exit air stream. Water activity was also successfully maintained close to the set point despite the massive production of water during the esterification process. Thus, the control system developed in this study is particularly useful for systems where large amounts of water are produced and where conventional methods make it difficult to control water activity as a result of a low water transfer rate. The effects that computer control of the water activity had on the reaction rate and yield were also examined. The reaction yield was significantly improved with water activity control. The conversions obtained at 28 h without and those with water activity control were 70% and 96%, respectively. In addition, from the fact that the final yields increased with decreasing a(w), computer-aided water activity control was performed with a set-point change. By controlling a(w) at 0.55 during initial reaction phase, followed by a step change of a(w) from 0.55 to 0 after 11 h of reaction, it was possible to enhance the final conversion to 100%.     

Computer-aided real-time estimation of reaction conversion for lipase-catalyzed esterification in solvent-free systems

Real-time conversion estimation through macroscopic balancing was investigated for enzymatic esterification reactions in a solvent-free system. In principle, the conversion of ester synthesis can be determined from the amount of water produced by the reaction because water is formed as a by-product in the same molar ratio as the product. In this study, we show that the water production rate, and thereby the reaction conversion, can be estimated on-line from measurements of the relative humidity of the inlet and outlet air and the material balances of water in the system. In order to test the performance of the real-time conversion estimation method, the lipase-catalyzed esterification reaction of n-capric acid and n-decyl alcohol in solvent-free media was conducted while controlling the water activity at various values. When the reaction conversions estimated on-line were compared with those analyzed off-line by gas chromatography, good agreement was obtained: the average mean absolute error was +/- 2.4% of the reaction conversion despite the simplicity of the method. The on-line estimation method presented here requires no expensive or complicated analytical instruments and no sampling of reaction medium. It can be used for monitoring nonaqueous enzymatic reactions where water is produced or consumed during reaction.     

Synthesis of triglycerides of phenylalkanoic acids by lipase-catalyzed esterification in a solvent-free system

Immobilized Candida antarctica lipase B catalyzed the synthesis of triglycerides from glycerol and phenylalkanoic acids in a solvent-free system. 4-Phenylbutyric acid was the best acyl donor and displayed the highest synthetic rate of triphenylbutyrin (glyceryl triphenylbutyrate) at 65 degrees C among various phenylalkanoic acids with straight alkyl chains. The external mass transfer between the immobilized lipase and the bulk reaction mixture was limited. Different methods of removing water during the lipase-catalyzed esterification including spontaneous evaporation, the use of saturated salts solutions, and the use of molecular sieves were studied. The highest yield of triphenylbutyrin at 65 degrees C was 98%, by the elimination of water using molecular sieves in a solvent-free system. The glycerol was almost completely esterified to triphenylbutyrin in excess phenylbutyric acid with various substrate molar ratios.     

Microwave accelerated solvent-free synthesis and antifungal evaluations of flavanones

Microwave irradiation of 2-hydroxy chalcones under solvent-free conditions resulted in a “green-chemistry” procedure for the preparation of flavanones in good yields, using an unmodified household microwave oven and silica as solid support. By irradiation of 2-hydroxy chalcones with trifluoroacetic acid over silica gel, 11 known flavanones were prepared in high yields. The synthesised compounds were characterised using spectroscopic techniques, namely, ¹H NMR, ¹³C NMR and IR, and screened for their antifungal activity in vitro against Sclerotium rolfsii and Rhizoctonia solani by poisoned food technique. The compounds tested were found to be more active against R. solani, whereas against S. rolfsii, moderate activity was observed, as evident from LC₅₀ values. The most potent compound 2-(4-fluorophenyl)-2,3-dihydrochromen-4-one (4a) had LC₅₀ value of 12.0 mg L^?1 followed by 11, 11a, 3a, 9a, 8a, 10a and 10 having LC₅₀ values 18.21, 18.3, 32.9, 50.7, 88.8, 118.8 and 119.7 mg L^?1, respectively.     

On-line conversion estimation for solvent-free enzymatic esterification systems with water activity control

On-line conversion estimation of enzymatic esterification reactions in solvent-free media was investigated. In principle, conversion to ester can be determined from the amount of water produced by the reaction, because water is formed as a by-product in a stoichiometric manner. In this study, we estimated the water production rate only from some measurements of relative humidity and water balances without using any analytical methods. In order to test the performance of the on-line conversion estimation, the lipase-catalyzed esterification ofn-capric acid andn-decyl alcohol in solvent-free media was performed whilst controlling water activity at various values. The reaction conversions estimated on-line were similar to those determined by offline gas chromatographic analysis. However, when the water activity was controlled at higher values, discrepancies between the estimated conversion values and the measured values became significant. The deviation was found to be due to the inaccurate measurement of the water content in the reaction medium during the initial stages of the reaction. Using a digital filter, we were able to improve the accuracy of the on-line conversion estimation method considerably. Despite the simplicity of this method, the on-line estimated conversions were in good agreement with the off-line measured values.     

Enzyme-catalysed production of n-butyl palmitate using ultrasound-assisted esterification of palmitic acid in a solvent-free system

Bioprocess and Biosystems Engineering - This work exhibits the implementation of ultrasound technology in solvent-free synthesis study of n-butyl palmitate using Fermase CALB™10000....     

Increased methyl esterification of membrane proteins in aged red-blood cells. Preferential esterification of ankyrin and band-4.1 cytoskeletal proteins

The enzymatic carboxyl methyl esterification of erythrocyte membrane proteins has been investigated in three different age-related fractions of human erythrocytes. When erythrocytes of different mean age, separated by density gradient centrifugation, were incubated under physiological conditions (pH 7.4, 37 degrees C) in the presence of L-[methyl-3H]methionine, the precursor in vivo of the methyl donor S-adenosylmethionine, a fourfold increase in membrane-protein carboxyl methylation was observed in the oldest cells compared with the youngest ones. The identification of methylated species, based on comigration of radioactivity with proteins stained with Coomassie blue, analyzed by sodium dodecyl sulfate/polyacrylamide gel electrophoresis, shows, in all cell fractions, a pattern similar to that reported for unfractionated erythrocytes. However in the membrane of the oldest erythrocytes the increase in methylation of the cytoskeletal proteins, bands 2.1 and 4.1, appears to be significantly more marked compared with that observed in the other methylated polypeptides. Furthermore the turnover rate of incorporated [3H]methyl groups in the membrane proteins of the oldest cells markedly increases during cell ageing. Particularly in band 4.1 the age-related increase in methyl esterification is accompanied by a significant reduction of the half-life of methyl esters. The activity of cytoplasmic protein methylase II does not change during cell ageing, while the isolated ghosts from erythrocytes of different age show an age-related increased ability to act as methyl-accepting substrates, when incubated in presence of purified protein methylase II and methyl-labelled S-adenosylmethionine, therefore the relevance of membrane structure in determining membrane protein methylation levels can be postulated. Finally the possible correlation of this posttranslational protein modification with erythrocyte ageing is discussed.     

Preparation of lipophilic alkyl (hydroxy)benzoates by solvent-free lipase-catalyzed esterification and transesterification

Agal-fermentation-based microbio-diesel production was realized through high-cell-density fermentation of Chlorella protothecoides and efficient transesterification process. Cell density achieved was 16.8 g l⁻¹ in 184 h and 51.2 g l⁻¹ in 167 h in a 5-l bioreactor by performing preliminary and improved fed-batch culture strategy, respectively. The lipid content was 57.8, 55.2, and 50.3% of cell dry weight from batch, primary, and improved fed-batch culture in 5-l bioreactor. Transesterification was catalyzed by immobilized lipase, and the conversion rate reached up to 98%. The properties of biodiesel from Chlorella were comparable to conventional diesel fuel and comply with US standard for Biodiesel. In a word, the approach including high-density fermentation of Chlorella and enzymatic transesterification process were set up and proved to be a promising alternative for biodiesel production.     

Secreted heat shock proteins in sunflower suspension cell cultures

Sunflower suspension cell cultures were subjected to different heat treatments and the electrophoretic patterns of heat-induced endocellular and secreted proteins were analyzed. In response to heat shock (3 h at 40°C), sunflower cells synthesized new polypeptides and secreted them into the medium, while the synthesis of other polypeptides was suppressed. Two major polypeptides of about 50 and 32 kDa were strongly induced. The two-dimensional electrophoretic analysis showed that the 32-kDa band is composed of at least four different polypeptides. Western blotting hybridizations of secreted proteins with various lectins were performed. The 32-kDa band gave a positive signal with concanavalin A. Received: 8 March 1996 / Revision received: 30 September 1996 / Accepted: 15 October 1996     

Enzymatic methyl esterification of Escherichia coli ribosomal proteins.

Enzymatic methyl ester formation in Escherichia coli ribosomal proteins was observed. Alkali lability of the methylated proteins and derivatization of the methyl groups as methyl esters of 3,5-dinitrobenzoate indicate the presence of protein methyl esters. The esterification reaction occurs predominantly on the 30S ribosomal subunit, with protein S3 as the major esterified protein. When the purified 30S subunit was used as the methyl acceptor, protein S9 was also found to be esterified. The enzyme responsible for the esterification of free carboxyl groups in proteins, protein methylase II (S-adenosyl-L-methionine:protein carboxyl methyltransferase, EC 2.1.1.24), was identified in E. coli Q13. This enzyme is extremely unstable when compared with that from mammalian origin. By molecular sieve chromatography, E. coli protein methylase II showed multiple peaks, with a major broad peak around 120,000 daltons and several minor peaks in the lower-molecular-weight region. Rechromatography of the major enzyme peak showed activities in several fractions that are much lower in molecular weight. The substrate specificity of the E. coli enzyme is similar to that of the mammalian enzyme. The Km value for S-adenosyl-L-methionine is 1.96 X 10(-6) M, and S-adenosyl-L-homocysteine was found to be a competitive inhibitor, with a Ki value of 1.75 X 10(-6) M.     

Analysis of solvent-free ethyl oleate enzymatic synthesis at equilibrium conditions

This work reports experimental equilibrium data for the esterification of pure oleic acid and a fatty acid mixture with ethanol, using an immobilized Candida antarctica B lipase as catalyst. Reactions are performed in a solvent-free system, containing a mixture of substrates and different amounts of distilled water. According to the initial amount of water and the extent of the reaction, one or two liquid phases are present. Therefore, when the equilibrium is achieved, the liquid–liquid and chemical reaction equilibria have to be simultaneously satisfied.

Several reports dealing with enzymatic reactions performed in two-phase systems have found that the value of the reaction equilibrium constant calculated from overall experimental concentrations varies not only with temperature but also with substrate ratio and water content. Although this approach is a valuable way to explore equilibrium shifts in biphasic systems, it is limited to ideal systems with constant partition coefficients. The aim of this work is to consider the biphasic nature of the reactive mixture through a computational procedure that simultaneously takes into account liquid–liquid and reaction equilibria. This approach enables the determination of a classical temperature-dependent thermodynamic equilibrium constant, which accurately fits experimental equilibrium conversions over a wide range of operating conditions.     

Retinoid-binding proteins and retinol esterification in cultured retinal pigment epithelium cells

The esterification of all-trans retinol and the occurrence of cytosolic retinoid-binding proteins was investigated in cultured bovine retinal pigment epithelium (RPE) cells. ³H-labeled all-trans retinyl ester (mainly palmitate) was formed at an initial rate of 0.1 nmol·mg protein⁻¹·min⁻¹ when ³H-labeled all-trans retinol was incubated with the 100,000 g pellet obtained from a homogenate of freshly-harvested cells. No esterification could be detected under the same conditions after 14 days in culture in defined medium (DM) or in medium containing 20% fetal bovine serum (CM). No enhancement or restoration of esterifying capacity was observed when the assay mixture was supplemented with palmitoyl CoA. As determined by specific, saturable binding of ³H-labeled all-trans retinol and ³H-labeled 11-cis retinal to proteins with mol. wts 16,000 and 33,000 dalton on calibrated Bio-Sil TSK 250 size-exclusion columns, the cytosol of freshly-harvested RPE cells contained cellular retinol-binding protein (CRBP) and cellular retinal-binding protein (CRAlBP). By comparison with the quantity of ³H-labeled all-trans retinol bound under identical conditions to pure dog liver CRBP, it was estimated that fresh RPE cells contained 102 ± 3 ng CRBP·μg cytosol protein⁻¹. In cultured and subcultured cells, CRBP was present at much lower levels (down to one-tenth of the initial amounts) and CRAlBP could not be detected. Since binding of ³H-labeled all-trans retinoic acid to a protein with molecular weight of 17,000 dalton was not observed in the cytosols of fresh or cultured cells, it was concluded that cellular retinoic acid binding protein (CRABP) was either present at very low levels or absent altogether. An unidentified peak of specific ³H-labeled all-trans-retinoic acid binding at mol. wt 61,000 dalton was prominent in subcultured cells. These results show that in RPE cells in culture the expression of differentiated phenotype with respect to retinoid utilization undergoes significant modification. It is postulated that changes in the composition of the extracellular matrix (e.g. absence of interstitial retinol-binding protein, IRBP) may be involved.     

Optimization of Candida sp. 99-125 lipase catalyzed esterification for synthesis of monoglyceride and diglyceride in solvent-free system

Esterification of glycerol and oleic acid catalyzed by lipase Candida sp. 99-125 was carried out to synthesize monoglyceride (MAG) and diglyceride (DAG) in solvent-free system. Beta-cyclodextrin as an assistant was mixed with the lipase powder. Six reaction variables, initial water content (0–14 wt% of the substrate mass), the glycerol/oleic acid molar ratio (1:1–6:1), catalyst load (3–15 wt% of the substrate mass), reaction temperature (30–60 °C), agitator speed (130–250 r/min) and beta-cyclodextrin/lipase mass ratio (0–2) were optimized. The optimal conditions to the synthesis of MAG and DAG were different: the optimal glycerol/oleic acid molar ratio, beta-cyclodextrin/lipase mass ratio, catalyst load and reaction temperature were 6:1, 0, 5%, 50 °C for MAG, and 5:1, 1.5, 10%, 40 °C for DAG, respectively. The optimal water content and agitator speed for both MAG and DAG were 10% and 190 r/min, respectively. Under the optimal conditions, 49.6% MAG and 54.3% DAG were obtained after 8 h and 4 h, respectively, and the maximum of 81.4% MAG plus DAG (28.1% MAG and 53.3% DAG) was obtained after 2 h under the DAG optimal condition. Above 90% purity of MAG and DAG can be obtained by silica column separation.     

Enzymatic conversion of sunflower oil to biodiesel in a solvent-free system: Process optimization and the immobilized system stability

The feasibility of using the commercial immobilized lipase from Candida antarctica (Novozyme 435) to synthesize biodiesel from sunflower oil in a solvent-free system has been proved. Using methanol as an acyl acceptor and the response surface methodology as an optimization technique, the optimal conditions for the transesterification has been found to be: 45 ^oC, 3% of enzyme based on oil weight, 3:1 methanol to oil molar ratio and with no added water in the system. Under these conditions, >99% of oil conversion to fatty acid methyl ester (FAME) has been achieved after 50 h of reaction, but the activity of the immobilized lipase decreased markedly over the course of repeated runs. In order to improve the enzyme stability, several alternative acyl acceptors have been tested for biodiesel production under solvent-free conditions. The use of methyl acetate seems to be of great interest, resulting in high FAME yield (95.65%) and increasing the half-life of the immobilized lipase by about 20.1 times as compared to methanol. The reaction has also been verified in the industrially feasible reaction system including both a batch stirred tank reactor and a packed bed reactor. Although satisfactory performance in the batch stirred tank reactor has been achieved, the kinetics in a packed bed reactor system seems to have a slightly better profile (93.6 ± 3.75% FAME yield after 8–10 h), corresponding to the volumetric productivity of 48.5 g/(dm³ h). The packed bed reactor has operated for up to 72 h with almost no loss in productivity, implying that the proposed process and the immobilized system could provide a promising solution for the biodiesel synthesis at the industrial scale.     

Tissue-specific expression of sunflower heat shock proteins in response to water stress

Accumulation of mRNA and synthesis of low-molecular-weight heat shock proteins (LMW HSPs) was investigated in water-stressed sunflower, under experimental conditions resulting in little or no thermal stress. Using probes and antibodies derived from developmentally expressed LMW HSPs, it was shown that homologous mRNAs and proteins accumulate in the stem and root of water-stressed plants. This expression is quantitatively comparable with the response to heat shock: protein and mRNA accumulate to similar, high, levels and persist for comparable times during recovery from either environmental stress. However, it is shown that LMW HSPs with different molecular weights and isoelectric points are expressed in response to heat shock or water stress. Furthermore in situ localizations show a differential tissue-specificity for the water-stress- and heat-shock-induced LMW HSPs. Whereas the latter are localized mostly around the xylem vessels in the stem, the water-stress-induced proteins accumulate in the fascicular and interfascicular cambium. The possible functional implications for this specific expression are discussed.     

改性黄原胶酯化条件的优化及结构的表征

为了提高黄原胶的速溶性和粘度,将黄原胶进行改性处理。将黄原胶与马来酸酐进行酯化反应,探讨了黄原胶与马来酸酐摩尔比、反应时间和反应温度等因素的影响,以取代度为指标,利用响应面方法确定,该酯化反应的最优条件为:黄原胶与马来酸酐摩尔比1∶11.5、反应时间24.4 h、反应温度66℃。对改性黄原胶进行红外光谱、光散射和X-射线衍射等结构表征,表明酯化改性成功,且进一步解释了速溶性和粘度提高的原因。改性黄原胶细胞毒性实验,显示无毒性。结果表明,改性黄原胶的速溶性和粘度有很大提高,0.2%改性黄原胶的速溶性和粘度较对照提高了近3倍,在食品、药品等领域具有潜在的应用价值。     

Bromodimethylsulfonium bromide (BDMS) mediated dithioacetalization of carbohydrates under solvent-free conditions

A variety of diethyl dithioacetals of sugars can be prepared in very good yields by the reaction of various monosaccharides with ethanethiol in the presence of 3 mol % bromodimethylsulfonium bromide (BDMS) at 0-5 °C. Similarly, dipropyl dithioacetal derivatives can also be obtained in good yields using propanethiol under identical reaction conditions. These dithioacetal derivatives were characterized by per-O-acetylation using silica gel-supported perchloric acid. The significant features of the present protocol are good-to-excellent yields, mild, clean, and solvent-free reaction conditions. This method is extremely suitable for the large-scale preparation of dithioacetal derivatives of various sugars.     

Methyl esterification of glutamic acid residues of methyl-accepting chemotaxis proteins in Bacillus subtilis.

The amino acid residue modified in the reversible methylation of Bacillus subtilis methyl-accepting chemotaxis proteins was identified as glutamic acid; methylation results in the formation of glutamate 5-methyl ester. Identification was made by comparing the behaviour of a 3H-labelled compound isolated from proteolytically hydrolysed methyl-accepting chemotaxis proteins labelled in vivo with that of authentic methylated amino acids by chromatographic and electrophoretic techniques. Also, the isolated compound on mild alkaline hydrolysis shows behaviour identical with that of authentic glutamate 5-methyl ester. [3H]Methanol released by mild alkaline hydrolysis was made to react with 3,5-dinitrobenzyl chloride to form [3H]methyl 3,5-dinitrobenzoate, which was identified by reverse-phase high-pressure liquid chromatography.     

Influence of the operating conditions on lipase-catalysed synthesis of ricinoleic acid estolides in solvent-free systems

In this work, the synthesis of ricinoleic acid estolides, also named polyricinoleic acid (PR), in two different solvent-free reaction systems, catalysed by immobilised Candida rugosa lipase is described. First, the esterification was performed in an open air jacketed batch reactor and the influence of amount of enzyme, temperature and initial water content was tested. The best results were obtained when 5 g of soaked immobilised derivative was used as biocatalyst, and the reaction was carried out at 40 °C. It was observed that environmental relative humidity plays an important role in the enzymatic synthesis of ricinoleic acid estolides and, given that this parameter takes on a wide range of values depending on the season, it is considered the main cause of the poor reproducibility achieved in the open air reactor. To solve this problem, the ricinoleic acid estolides were synthesised under controlled atmosphere in a vacuum reactor with dry air intake. The optimum drying time of 7 h was selected. In these conditions, PR with an acid value of 57.5 mg KOH/g was synthesised in 48 h of reaction and the results were entirely reproducible.