Enzymatic Synthesis of Ethyl-glucoside Monooleate with Lipase in Solvent-free Medium

Ethylglucoside monooleate was synthesized by esterification between ethylglucoside and oleic acid with immobilized lipase from Candida antarctica in a solvent-free system. It was shown that a stirred tank reactor was suitable for the enzymatic reaction process involving substrates with low miscibility, in which the biocatalyst was recycled five times without significant activity loss. Removal of the co-product, water, from the reaction medium by carrying out the reaction under reduced pressure benefited the esterification reaction and increased the monooleate yield up to 97% within 8 hours.     

Improved synthesis of 1,3-diolein by Novozym 435-mediated esterification of monoolein with oleic acid

We successfully developed an efficient and promising bioprocess for 1,3-diolein synthesis by performing Novozym 435-mediated esterification of oleic acid with monoolein in this work. Under the optimized conditions (60 °C, molar ratio of oleic acid to monoolein 1.2:1), a 1,3-diolein yield of 93.7% could be achieved, and the yield of 1,2-diolien was low (2.6%). The high yield of 1,3-diolein and the optimum reaction time were improved remarkably compared with the results of our previous study, which involved the enzymatic esterification of oleic acid with glycerol. An additional advantage of the new process is the fact that 90% original activity of the enzyme was maintained after being used for 100 reactions. The present work could be seen as a useful enzyme-catalyzed process for the industrial production of 1,3-diacylglycerol.     

Enzymatic Synthesis of Ethyl-glucoside Monooleate with Lipase in Solvent-free Medium

Ethylglucoside monooleate was synthesized by esterification between ethylglucoside and oleic acid with immobilized lipase from Candida antarctica in a solvent-free system. It was shown that a stirred tank reactor was suitable for the enzymatic reaction process involving substrates with low miscibility, in which the biocatalyst was recycled five times without significant activity loss. Removal of the co-product, water, from the reaction medium by carrying out the reaction under reduced pressure benefited the esterification reaction and increased the monooleate yield up to 97% within 8 hours.     

The study of volt-ampere characteristics of ionic channels formed by gramicidin A

A method of measurement of the non-linearity coefficient of volt-ampere characteristics of the type i(U) approximately = U(1 + beta U2) has been developed for ionic channels formed by gramicidin A, using the third harmonic of the membrane current. The shape of the volt-ampere characteristics (VA) of ionic channels formed by gramicidin A did not depend on the antibiotic concentration in the membrane. The coefficient beta of non-linearity of VA of membranes modified by gramicidin A depended on electrolyte concentration "c" and it increased proportionally with the lg c from -17 V-2 at 0.03 mol/l KC1 to 8 V-2 at 3.4 mol/l KCl, and it was zero at co = 0.3 - 1 mol/l KCl. Egg lecithin and glycerol monooleate (GMO) membranes differ in their co values. The substitution of K+ for Li+ of the membrane solvent (n-heptane for n-hexadecane) did not influence the value of beta; the same applied for GMO membranes without any solvent. In a number of membranes, spontaneous change of the non-linearity coefficient with time observed after the membrane formation, as well as jumps of the non-linearity coefficient at a practically unchanged membrane conductivity. An analysis of some theoretical models of the ion transport through the channel has shown that, at voltages above 200 mV, these models provide rather small values of beta, or extremely high VA non-linearity.     

Photon correlation spectroscopy of bilayer lipid membranes

Light scattering by thermal fluctuations on simple monoglyceride bilayer membranes has been used to investigate the viscoelastic properties of these structures. Spectroscopic analysis of these fluctuations (capillary waves) permits the nonperturbative measurement of the interfacial tension and a shear interfacial viscosity acting normal to the membrane plane. The methods were established by studies of solvent and nonsolvent bilayers of glycerol monooleate (GMO). Changes in the tension of GMO/n-decane membranes induced by altering the composition of the parent solution were detected and quantified. In a test of the reliability of the technique controlled variations of the viscosity of the aqueous bathing solution were accurately monitored. The technique was applied to solvent-free bilayers formed from dispersions of GMO in squalane. The lower tensions observed attested to the comparative absence of solvent in such bilayers. In contrast to the solvent case, the solvent-free membranes exhibited a significant transverse shear viscosity, indicative of the enhanced intermolecular interactions within the bilayer.     

Optimisation and Characterisation of Lipase-Catalysed Synthesis of a Kojic Monooleate Ester in a Solvent-Free System by Response Surface Methodology

Kojic acid is widely used to inhibit the browning effect of tyrosinase in cosmetic and food industries. In this work, synthesis of kojic monooleate ester (KMO) was carried out using lipase-catalysed esterification of kojic acid and oleic acid in a solvent-free system. Response Surface Methodology (RSM) based on central composite rotatable design (CCRD) was used to optimise the main important reaction variables, such as enzyme amount, reaction temperature, substrate molar ratio, and reaction time along with immobilised lipase from Candida Antarctica (Novozym 435) as a biocatalyst. The RSM data indicated that the reaction temperature was less significant in comparison to other factors for the production of a KMO ester. By using this statistical analysis, a quadratic model was developed in order to correlate the preparation variable to the response (reaction yield). The optimum conditions for the enzymatic synthesis of KMO were as follows: an enzyme amount of 2.0 wt%, reaction temperature of 83.69°C, substrate molar ratio of 1:2.37 (mmole kojic acid:oleic acid) and a reaction time of 300.0 min. Under these conditions, the actual yield percentage obtained was 42.09%, which is comparably well with the maximum predicted value of 44.46%. Under the optimal conditions, Novozym 435 could be reused for 5 cycles for KMO production percentage yield of at least 40%. The results demonstrated that statistical analysis using RSM can be used efficiently to optimise the production of a KMO ester. Moreover, the optimum conditions obtained can be applied to scale-up the process and minimise the cost.     

Effect of PEG and other additives on cyclodextrin production by Bacillus macerans cyclomaltodextrin-glycosyl-transferase

Summary The effect of PEG and other polyols additives on cyclodextrins (CDs) production by Bacillus macerons cyclomaltodextrin-glycosyl-transferase (CGTase) was investigated. Mannitol, glycerol and PEG-200 (20%,v/v) enhanced the enzymatic production yield regardless of substrate concentration. Furthermore, the PEG-200 addition increased the thermostability of the CGTase.     

Production of 1,3-propanediol by <Emphasis Type="Italic">Clostridium butyricum</Emphasis> VPI 3266 using a synthetic medium and raw glycerol

Growth inhibition of Clostridium butyricum VPI 3266 by raw glycerol, obtained from the biodiesel production process, was evaluated. C. butyricum presents the same tolerance to raw and to commercial glycerol, when both are of similar grade, i.e. above 87% (w/v). A 39% increase of growth inhibition was observed in the presence of 100 g l^–1 of a lower grade raw glycerol (65% w/v). Furthermore, 1,3-propanediol production from two raw glycerol types (65% w/v and 92% w/v), without any prior purification, was observed in batch and continuous cultures, on a synthetic medium. No significant differences were found in C. butyricum fermentation patterns on raw and commercial glycerol as the sole carbon source. In every case, 1,3-propanediol yield was around 0.60 mol/mol glycerol consumed.     

膜融合剂对脂质体及血影膜膜流动性的影响

本文用荧光探针ANS,DPH与A研究了几种膜融合剂对脂质体与血影膜流动性的影响.蔗糖使PS脂质体的脂双层流动性降低,探针越是在极性区流动性越小,说明蔗糖主要作用于脂双层的极性区;蔗糖也使血影膜流动性降低,此作用是可逆的.油酸甘油脂(GMO)使PS脂质体的流动性增加,且越是在疏水区内部,流动性增加得越大,说明GMO主要是作用于脂双层的非极性区:GMO也使血影膜流动性增加,此作用是不可逆的.二甲亚砜(DMSO)对血影膜的作用,两种不同荧光探针不一样,对DPH的作用出现双相让,低浓度与高浓度的作用结果分别与蔗糖和GMO的作用一致.     

不同发酵条件下产甘油假丝酵母有机酸代谢的研究

产甘油假丝酵母 (Candidaglycerolgenesis)发酵产生的有机酸对丙三醇产品质量和产率均有影响。发现在发酵其它条件恒定 ,装液比和玉米浆浓度增加时 ,发酵液总酸是递增的。在装液比为 0 2和玉米浆浓度为 8g L时 ,丙酮酸和乳酸在细胞生长期可分别积累达 4 1g L和 1 0g L ,比正常发酵时增加 2倍以上 ,丙三醇产率也低 ;然而 ,装液比为 0 0 8和玉米浆浓度为 4g L时 ,丙酮酸和乳酸产生较低 ,丙三醇产率较高 ,但乙酸积累比供氧不足时高 ,可达 2 6g L。发酵过程中有机酸被细胞代谢 ,含量逐渐下降 ,如在初糖浓度为 1 0 0g L时 ,有机酸在细胞生长期积累至高峰后 ,丙三醇和有机酸随之均降低至较低含量 ,并且丙酮酸或乳酸可以转化为乙酸。此外 ,在外加一些添加剂时对其产生有机酸也有影响 ,如添加 1 %油酸和VB1时可以降低乙酸的积累 ,同时增加丙酮酸的含量 ,丙三醇产量也有所增加 ;而丙酮酸结构类似物氟代丙酮酸和亚硫酸盐促进乙酸的产生 ,使酮戊二酸合成减少 ,丙三醇产量约增加 2 0 %。     

Study of two-stage processes for the microbial production of 1,3-propanediol from glucose

The microbial production of 1,3-propanediol (1,3-PD) from glucose was studied in a two-stage fermentation process on a laboratory scale. In the first stage, glucose was converted to glycerol either by the osmotolerant yeast Pichia farinosa or by a recombinant Escherichia coli strain. In the second stage, glycerol in the broth from the first stage was converted to 1,3-PD by Klebsiella pneumoniae. The culture broth from P. farinosa was shown to contain toxic metabolites that strongly impair the growth of K. pneumoniae and the formation of 1,3-PD. Recombinant E. coli is more suitable than P. farinosa for producing glycerol in the first stage. The fermentation pattern from glycerol can be significantly altered by the presence of acetate, leading to a significant reduction of PD yield in the second stage. However, in the recombinant E. coli culture acetate formation can be prevented by fed-batch cultivation under limiting glucose supply, resulting in an effective production of 1,3-PD in the second stage with a productivity of 2.0 g l(-1) h(-1) and a high yield (0.53 g/g) close to that of glycerol fermentation in a synthetic medium. The overall 1,3-PD yield from glucose in the two stage-process with E. coli and K. pneumoniae reached 0.17 g/g.     

Process for biodiesel production from Cryptococcus curvatus

The objective of the current report is process optimization for economical production of lipids by the well known oleaginous yeast Cryptococcus curvatus and conversion of the lipids to biodiesel. A high cell density fed-batch cultivation on low cost substrate viz. crude glycerol resulted in a dry biomass and oil yield of up to 69 g/L and 48% (w/w), respectively. The process was scaled up easily to 26 L. The oil extraction process was also optimized using environmentally safe solvents. The oil profile indicated a high oleic acid content followed by palmitic acid, stearic acid and linoleic acid. The oil was trans-esterified to biodiesel and thoroughly characterized. This is the first end to end report on production of biodiesel from the C. curvatus oil.     

Functional cello-oligosaccharides production from the corncob residues of xylo-oligosaccharides manufacture

An integrated process has been developed, consisting of the “adsorption–separation” of cellulase enzymes to selectively remove β-glucosidase, and multi-stage enzymatic hydrolysis of corncob residues from xylo-oligosaccharides manufacture with the β-glucosidase deficient cellulase, aiming to obtain a high yield of cello-oligosaccharides production. After the “adsorption–separation” process, 79.50% of the endo-glucanase was retained in substrate, whereas 90.67% of β-glucosidase was removed with the separated liquid fraction, utilizing the different adsorbability of these enzymes to the substrate. A three-stage enzymatic hydrolysis of corncob residues with the β-glucosidase deficient cellulase was proposed in which the first, the second and the third stage were conducted for 6, 6 h and 12 h, respectively. Analysis indicated that the removal of hydrolysis products (glucose and cello-oligosaccharides) at each stage improved cello-oligosaccharides productivity and enzymatic hydrolysis yield. The cello-oligosaccharides yield and enzymatic hydrolysis yield in three-stage enzymatic hydrolysis were significantly improved to 51.78% and 75.56%, respectively, which were 36.00% and 25.10% higher than single-stage hydrolysis with original cellulase enzymes.     

Ethanol fermentation in an immobilized cell reactor using Saccharomyces cerevisiae

Fermentation of sugar by Saccharomyces cerevisiae, for production of ethanol in an immobilized cell reactor (ICR) was successfully carried out to improve the performance of the fermentation process. The fermentation set-up was comprised of a column packed with beads of immobilized cells. The immobilization of S. cerevisiae was simply performed by the enriched cells cultured media harvested at exponential growth phase. The fixed cell loaded ICR was carried out at initial stage of operation and the cell was entrapped by calcium alginate. The production of ethanol was steady after 24 h of operation. The concentration of ethanol was affected by the media flow rates and residence time distribution from 2 to 7 h. In addition, batch fermentation was carried out with 50 g/l glucose concentration. Subsequently, the ethanol productions and the reactor productivities of batch fermentation and immobilized cells were compared. In batch fermentation, sugar consumption and ethanol production obtained were 99.6% and 12.5% v/v after 27 h while in the ICR, 88.2% and 16.7% v/v were obtained with 6 h retention time. Nearly 5% ethanol production was achieved with high glucose concentration (150 g/l) at 6 h retention time. A yield of 38% was obtained with 150 g/l glucose. The yield was improved approximately 27% on ICR and a 24 h fermentation time was reduced to 7 h. The cell growth rate was based on the Monod rate equation. The kinetic constants (K(s) and mu(m)) of batch fermentation were 2.3 g/l and 0.35 g/lh, respectively. The maximum yield of biomass on substrate (Y(X-S)) and the maximum yield of product on substrate (Y(P-S)) in batch fermentations were 50.8% and 31.2% respectively. Productivity of the ICR were 1.3, 2.3, and 2.8 g/lh for 25, 35, 50 g/l of glucose concentration, respectively. The productivity of ethanol in batch fermentation with 50 g/l glucose was calculated as 0.29 g/lh. Maximum production of ethanol in ICR when compared to batch reactor has shown to increase approximately 10-fold. The performance of the two reactors was compared and a respective rate model was proposed. The present research has shown that high sugar concentration (150 g/l) in the ICR column was successfully converted to ethanol. The achieved results in ICR with high substrate concentration are promising for scale up operation. The proposed model can be used to design a lager scale ICR column for production of high ethanol concentration.     

Production of diacylglycerols from glycerol monooleate and ethyl oleate through free and immobilized lipase-catalyzed consecutive reactions

The ability of free and immobilized lipase on the production of diacylglycerols (DAG) by transesterification of glycerol monooleate (GMO) and ethyl oleate was investigated. Among three free lipases such as lipase G (Penicillium cyclopium), lipase AK (Pseudomonas fluorescens) and lipase PS (Pseudomonas cepacia), lipase PS exhibited the highest DAG productivity, and the DAG content gradually increased up to 24 hours reaction and then remained steady. The comparative result for DAG productivity between free lipase PS and immobilized lipases (lipase PS-D and Lipozyme RM IM) during nine times of 24 hours reaction indicated that total DAG production was higher in immobilized lipase PS-D (183.5mM) and Lipozyme RM IM (309.5mM) than free lipase PS (122.0mM) at the first reaction, and that the DAG production rate was reduced by consecutive reactions, in which more sn-1,3-DAG was synthesized than sn-1,2-DAG. During the consecutive reactions, the activity of lipase PS was relatively steady by showing similar DAG content, whereas DAG production of lipase PS-D and Lipozyme RM IM was gradually decreased to 69.9 and 167.1mM at 9th reaction, respectively, resulting in 62% and 46% reduced production when compared with 1st reaction. Interestingly, from 7th reaction lipase PS produced more DAG than immobilized lipase PS-D, and exhibited a stable activity for DAG production. Therefore, the present study suggested that DAG productivity between GMO and ethyl oleate was higher in immobilized lipases than free lipases, but the activity was reduced with repeated uses.     

Effect of particle size on the rate of enzymatic hydrolysis of cellulose

The effect of particle size on enzymatic hydrolysis of cellulose has been investigated. The average size of microcrystalline cotton cellulose has been reduced to submicron scale by using a media mill. The milled products were further subjected to hydrolysis using cellulase. High cellulose concentration (7%) appeared to retard the size reduction and resulted in greater particles and smaller specific surface areas than those at low concentration (3%) with the same milling time. Initial rate method was employed to explore the rate of enzymatic hydrolysis of cellulose. The production rate of cellobiose was increased at least 5-folds due to the size reduction. The yield of glucose was also significantly increased depending upon the ratio of enzyme to substrate. A high glucose yield (60%) was obtained in 10-h hydrolysis when the average particle size was in submicron scale.     

γ-decalactone production by Yarrowia lipolytica and Lindnera saturnus in crude glycerol

Flavor compounds are commonly obtained from chemical synthesis or extracted from plants. These sources have disadvantages, such as racemic mixture generation, more steps to yield the final product, low yield, and high cost, making the microbial fermentation an alternative and potential way to obtain flavor compounds. The most important lactone for flavor application is γ-decalactone, which has an aroma of peach and can be obtained by ricinoleic acid biotransformation through yeast peroxisomal β-oxidation. The aim of this work was to use crude glycerol, a residual biodiesel industry, for the production of bioaroma from two different yeasts. Yarrowia lipolytica CCMA 0357 and Lindnera saturnus CCMA 0243 were grown at different concentrations (10, 20, and 30% w/v) of substrates (castor oil and crude glycerol) for γ-decalactone production. L. saturnus CCMA 0243 produced higher concentration of y-decalactone (5.8?g/L) in crude glycerol, whereas Y. lipolytica CCMA 0357 showed a maximum production in castor oil (3.5?g/L). Crude glycerol showed better results for γ-decalactone production when compared to castor oil. L. saturnus CCMA 0243 has been shown to have a high potential for γ-decalactone production from crude glycerol.     

Application of high hydrostatic pressure for increasing activity and stability of enzymes

Elevated hydrostatic pressure has been used to increase catalytic activity and thermal stability of alpha-chymotrypsin (CT). For an anilide substrate, characterized by a negative value of the reaction activation volume (DeltaV( not equal)), an increase in pressure at 20 degrees C results in an exponential acceleration of the hydrolysis rate catalyzed by CT reaching a 6.5-fold increase in activity at 4700 atm (4.7 kbar). Due to a strong temperature dependence of DeltaV( not equal), the acceleration effect of high pressure becomes more pronounced at high temperatures. For example, at 50 degrees C, under a pressure of 3.6 kbar, CT shows activity which is more than 30 times higher than the activity at normal conditions (20 degrees C, 1 atm). At pressures of higher than 3.6 kbar, the enzymatic activity is decreased due to a pressure-induced denaturation.Elevated hydrostatic pressure is also efficient for increasing stability of CT against thermal denaturation. For example, at 55 degrees C, CT is almost instantaneously inactivated at atmospheric pressure, whereas under a pressure of 1.8 kbar CT retains its anilide-hydrolyzing activity during several dozen minutes. Additional stabilization can be achieved in the presence of glycerol, which is most effective for protection of CT at an intermediate concentration of 40% (v/v). There has been observed an additivity in stabilization effects of high pressure and glycerol: thermal inactivation of pressure-stabilized CT can be decelerated in a supplementary manner by addition of 40% (v/v) glycerol. The protection effect of glycerol on the catalytic activity and stability of CT becomes especially pronounced when both extreme factors of temperature and pressure reach critical values. For example, at approximately 55 degrees C and 4.7 kbar, enzymatic activity of CT in the presence of 40% (v/v) glycerol is severalfold higher than in aqueous buffer.The results of this study are discussed in terms of the hypotheses which explain the action of external and medium effects on protein structure, such as preferential hydration and osmotic pressure. (c) 1996 John Wiley & Sons, Inc.     

Optimization of polyphenol extraction from red grape pomace using aqueous glycerol/tartaric acid mixtures and response surface methodology

Grape pomace is a food industry waste containing a high burden of antioxidant polyphenols and several methodologies have been developed for their efficient extraction. However, a sustainable and environmentally friendly process should involve recovery means composed of benign, non-toxic solvents, such as tartaric acid and glycerol, which are natural food constituents. In this line, this study examined the extraction of polyphenols using aqueous tartaric acid/glycerol solutions. The aim was to assess the role of acid and glycerol concentration in the extraction yield, employing a Box-Behnken experimental design and response surface methodology. The results showed that solutions containing only glycerol (20%, w/v) are more suitable for retrieving polyphenols, flavonoids, and pigments from grape pomace, while tartaric acid exerted a negative effect in this regard, when tested at concentrations up to 2% (w/v).     

Continuous production of monoacylglycerols from palm olein in packed-bed reactor with immobilized lipase PS

A packed-bed reactor (PBR) system using immobilized lipase PS as biocatalyst was developed for continuous monoacylglycerols (MAG) production. The condition for continuous MAG production using immobilized lipase PS (IM-PS) of 1.5 g (550 U) in PBR (0.68 cm i.d., 25 cm long) was optimized. The effect of molar ratio of glycerol to palm olein, water content in glycerol and residence time on MAG production was investigated. The optimal glycerol to palm olein molar ratio and water content in glycerol were 12:1 and 10% (w/w), respectively. The yield of MAG increased with increasing residence time. At a residence time of 7.5 h gave the highest yield of MAG of 60%. The long-term operation gave the highest yield of MAG 61.5% at 24 h of the operation time with the productivity of 1.61 g MAG/day. A half-life of the long-term process was 35 days of the operation time with the productivity of 0.81 g MAG/day. Furthermore, the large scale of MAG production was performed continuously with IM-PS of 15 g (5500 U) in PBR (1.5 cm i.d., 50 cm long). The highest yield of MAG in large-scale operation of 70.1% and the 11-fold increasing in productivity of 18.3 g MAG/day were obtained at 24 h of the operation time.