Purification of l-(+)-lactic acid from pre-treated fermentation broth using vapor permeation-assisted esterification

The vapor permeation-assisted esterification of l-(+)-lactic acid and ethanol was investigated using a zeolite membrane. Pervaporation and vapor permeation were initially investigated for dehydration performances, and the latter showed much better results. The molecular sieve property of the membrane resulted in a high separation factor of over 1000 for all conditions. The maximum flux was 10.24 kg/(m² h) at a feed temperature of 145 °C, a water feed concentration of 10 wt%, and a feed pressure of 4.0 bars, respectively. For vapor permeation-assisted esterification using synthetic solutions, the productivity and ethyl lactate yield strongly depended on the dehydration rate. Realistic purifications were performed with fermentation broths of Pediococcus pentosaceus as the lactic acid producer. Experimental results revealed that most of the lactic acid was converted into ethyl lactate at the final stage of the reaction. After distillation and hydrolysis, high purity l-(+)-lactic acid was obtained with more than 95% recovery yields.     

Effect of water on methanolysis of glycerol trioleate catalyzed by immobilized lipase Candida sp. 99–125 in organic solvent system

In this study, hydrolysis and methanolysis of glycerol trioleate (TG) by lipase Candida sp. 99–125 were investigated under different water conditions. Both the reaction rates were relatively low without water, while increasing water content to 5 wt.% (or more, from 10–20%) based on the TG amount caused remarkable higher TG conversion for both reactions. Moreover, comparing the time course curves of the hydrolysis and methanolysis, it could be concluded that the methanolysis reaction catalyzed by this Candida sp. 99–125 appeared to accord with the successive reaction mechanism. TG was first hydrolyzed to partial glycerides and oleic acid (OA), then oleic acid methyl ester (OAME) was produced by esterification of the OA with methanol. This water effect was also confirmed by the experiments that water substitutions such as t-butanol and some surfactants added into the system did not get such high yields as that of the water included system. So these results showed that water took part in the methanolysis reaction, and successive hydrolysis–esterification process might be the catalytic mechanism of this lipase.     

Effects of water on biodiesel fuel production by supercritical methanol treatment

In the conventional transesterification of fats/vegetable oils for biodiesel production, free fatty acids and water always produce negative effects, since the presence of free fatty acids and water causes soap formation, consumes catalyst and reduces catalyst effectiveness, all of which result in a low conversion. The objective of this study was, therefore, to investigate the effect of water on the yield of methyl esters in transesterification of triglycerides and methyl esterification of fatty acids as treated by catalyst-free supercritical methanol. The presence of water did not have a significant effect on the yield, as complete conversions were always achieved regardless of the content of water. In fact, the present of water at a certain amount could enhance the methyl esters formation. For the vegetable oil containing water, three types of reaction took place; transesterification and hydrolysis of triglycerides and methyl esterification of fatty acids proceeded simultaneously during the treatment to produce a high yield. These results were compared with those of methyl esters prepared by acid- and alkaline-catalyzed methods. The finding demonstrated that, by a supercritical methanol approach, crude vegetable oil as well as its wastes could be readily used for biodiesel fuel production in a simple preparation.     

Highly efficient transformation of waste oil to biodiesel by immobilized lipase from Penicillium expansum

An inexpensive self-made immobilized lipase from Penicillium expansum was shown to be an efficient biocatalyst for biodiesel production from waste oil with high acid value in organic solvent. It was revealed that water from the esterification of free fatty acids and methanol prohibited a high methyl ester yield. Adsorbents could effectively control the concentration of water in the reaction system, resulting in an improved methyl ester yield. Silica gel was proved to be the optimal adsorbent, affording a ME yield of 92.8% after 7 h. Moreover, the enzyme preparation displayed a higher stability in waste oil than in corn oil, with 68.4% of the original enzymatic activity retained after being reused for 10 batches.     

Effect of several factors on soluble lipase-mediated biodiesel preparation in the biphasic aqueous-oil systems

Biodiesel is increasingly perceived as an important component of solutions to the important current issues of fossil fuel shortages and environmental pollution. Utilization of soluble lipase offers an alternative approach to lipase-catalyzed biodiesel production using immobilized enzyme or whole-cell catalysis. Soluble lipase NS81020, produced by submerged fermentation of genetically modified Aspergillus oryzae microorganism, was first proposed here as the catalyst of biodiesel preparation with oleic acid in the biphasic aqueous-oil systems. The effect factors such as enzyme concentration, water content, temperature, molar ratio of methanol to oil, stirring rate and pH of buffer solution on the esterification rate were investigated systematically. The reaction time could be shortened with the increasing of enzyme concentration as long as the maximum enzyme absorptive capacity on the interface in the biphasic aqueous-oil systems was not achieved. The optimal water content in the biphasic aqueous-oil systems was 10 wt% by oleic acid weight. The reaction rate was enhanced with the increasing molar ratio of methanol to oil, the increasing stirring rate or the decreasing temperature. Although soluble lipase NS81020 had lower activity at pH 10.55, hydroxyl ion conduced to restrain hydrolysis of methyl ester and facilitated the reaction toward the methyl ester formation.     

On the reactivity of carboxyl groups of ribonuclease-A in anhydrous methanol.

The esterification of Ribonuclease-A in methanol/0.1 M hydrochloric acid has been studied by measuring the decrease in the number of titratable groups of the protein and estimating the amount of methanol incorporated. Esterification of nearly five of the 11 free carboxyl groups of the protein resulted in almost complete inactivation of the enzyme. The initial products of esterification have been chromatographed on Amberlite columns, and five partially active methyl ester derivatives of Ribonuclease-A have been isolated. The dimethyl ester, the initial product of esterification with reduced catalytic activity, has the carboxyl groups of Glu-49 and Asp-53 modified. Even in the non-aqueous solvent, as in the native structure of the protein in aqueous solution, these carboxyl groups are the fast reacting ones. Subsquently, the esterification reaction appears to proceed preferentially at the C-terminal region of the molecule. Comparison of the reactivities of carboxyl groups of Ribonuclease-A in acidic methanol to that known in aqueous solutions (with carbodiimides) suggests that the structure of Ribonuclease-A in the non-aqueous solvent resembles, at least in part, the structure in aqueous environment.     

Biodiesel production by supercritical process with crude bio-methanol prepared by wood gasification

In order to prepare a genuine biodiesel, it is essential to use methanol prepared from biomass but not natural gas for biodiesel production. Thus, we have proposed to use crude bio-methanol produced by wood gasification for biodiesel production. Since such a bio-methanol contains some impurities, an effect of its impurities was studied on the biodiesel production by supercritical method. In general, impurities in crude bio-methanol are reported to include methyl formate, ethanol, 1-butanol, diisopropyl ether, water, etc. Triglycerides and oleic acids were, thus, treated with these impurities under supercritical conditions. As a result, it was found that methyl formate, ethanol and 1-butanol could convert them to fatty acid alkyl esters (BDF), whereas no conversion was achieved with diisopropyl ether. Thus, crude bio-methanol can be used for BDF production as a substitute for methanol from fossil resources. However, due to more efficient reaction, crude bio-methanol can be more applicable to the two-step supercritical methanol process, consisting of hydrolysis of triglycerides and subsequent esterification of fatty acids, compared with the one-step supercritical methanol process, where transesterification of triglycerides is a major reaction.     

Lipase-Catalyzed Synthesis and Hydrolysis of Cholesterol Oleate in Aot/Isooctane Microemulsions

We have examined a lipase-catalyzed bidirectional ester synthesis/hydrolysis reaction in a water-in-oil microemulsion system. The reactants were cholesterol (alcohol), oleic acid (acid) and cholesterol oleate (ester), and the solvent system consisted of sodium bis(2-ethylhexyl)sulfosuccinate (AOT)/isooctane/water. The reactions were assayed by using [³H]oleic acid, [³H]cholesterol, or [³H]cholesterol oleate for the synthesis and hydrolysis reactions, respectively (separate incubations). The lipase that we used derived from Candida cylindracea, and was used at a concentration of 0.1mg/ml microemulsion. The reactions were performed at 22°C as the reactions proceeded more slowly at higher temperatures. With the initial reactant concentrations set to 10 mM cholesterol, 1 min oleic acid, and 1 mM cholesterol oleate, it was observed that the optimal [H₂O]/[AOT] ratio was at about 9 both for the esterification reaction and for the hydrolysis reaction (after 24 h). The hydrolysis reaction was slower than the synthesis reaction at all [H₂O]/[AOT] ratios studied (0-20), but the difference in reaction yield for the synthesis and the hydrolysis reactions became smaller as the reaction time increased (up to 11 days). When the reaction yield was followed as a time function, it was observed that about 80% of the oleic acid was esterified within 3 days of reaction ([H₂O]/[AOT] ratio of 6), whereas the corresponding value of 80% hydrolysis of cholesterol oleate was reached within 11 days. The results of the present study indicate that by choosing optimal reactant concentrations and reaction conditions, it is at least in part possible to determine the direction of the lipase-catalyzed synthesis/hydrolysis reaction.     

Preparation of o-palmitoyl alkyl lactates through lipase atalysis

Preparation of o-palmitoyl alkyl lactates with methyl, ethyl, propyl, isopropyl and butyl lactates were attempted in a complex esterification reaction using lipases as catalysts. Compared to lactic acid, alkyl lactates were found to be less inhibitory in nature as they resulted in slightly better yields at shake-flask level. Of the alkyl lactates tested, butyl lactate showed better esterification. Porcine pancreas lipase gave higher yields of esters than Rhizomucor miehei lipase (Lipozyme IM20).     

Production of biodiesel and lactic acid from rapeseed oil using sodium silicate as catalyst

Biodiesel and lactic acid from rapeseed oil was produced using sodium silicate as catalyst. The transesterification in the presence of the catalyst proceeded with a maximum yield of 99.6% under optimized conditions [3% (w/w) sodium silicate, methanol/oil molar ratio 9/1, reaction time 60 min, reaction temperature 60 °C, and stirring rate 250 rpm]. After six consecutive transesterification reactions, the catalyst was collected and used for catalysis of the conversion of glycerol to lactic acid. A maximum yield of 80.5% was achieved when the reaction was carried out at a temperature of 300 °C for 90 min. Thus, sodium silicate is an effective catalyst for transesterification and lactic acid production from the biodiesel by-product, glycerol.     

Biodiesel production from high acid value waste frying oil catalyzed by superacid heteropolyacid

Transesterification of waste cooking oil with high acid value and high water contents using heteropolyacid H3PW12O40 x 6H2O (PW12) as catalyst was investigated. The hexahydrate form of PW(12) was found to be the most promising catalyst which exhibited highest ester yield 87% for transesterification of waste cooking oil and ester yield 97% for esterification of long-chain palmitic acid, respectively. The PW12 acid catalyst shows higher activity under the optimized reaction conditions compared with conventional homogeneous catalyst sulfuric acid, and can easily be separated from the products by distillation of the excess methanol and can be reused more times. The most important feature of this catalyst is that the catalytic activity is not affected by the content of free fatty acids (FFAs) and the content of water in the waste cooking oil and the transesterification can occur at a lower temperature (65 degrees C), a lower methanol oil ratio (70:1) and be finished within a shorter time. The results illustrate that PW12 acid is an excellent water-tolerant and environmentally benign acid catalyst for production of biodiesel from waste cooking oil.     

Mechanism study on NS81006-mediated methanolysis of triglyceride in oil/water biphasic system for biodiesel production

Compared to immobilized lipase, soluble lipase has the merits of lower cost and faster reaction rate, thus much attention has been paid to soluble lipase-mediated methanolysis for biodiesel (fatty acid methyl ester, FAME) production in recent years. Our previous study showed that soluble lipase NS81006 could effectively catalyze the methanolysis of soybean oil (triglyceride, TG) for FAME preparation in oil/water biphasic system. Study on the related mechanism of soluble lipase NS81006-mediated methanolysis of TG was carried out in this paper. Based on the analysis of substances change in the reaction process, mechanism model was hypothesized and the model parameters were simulated by Matlab. The simulated model was validated further. The results showed that in the reaction process of soluble lipase NS81006-mediated methanolysis of TG in oil/water biphasic system, TG proceeded three-step hydrolysis to generate FFA (free fatty acid), and then FFA transformed into FAME by esterification with methanol. During the whole process, FFA is mainly generated through the hydrolysis of TG and intermediate DG (diglyceride), while the hydrolysis of FAME could be ignored.     

Improvement of the enantioselectivity of lipase-catalyzed naproxen ester hydrolysis in organic solvent

A method is presented to improve the enantioselectivity of lipase-catalyzed hydrolysis of naproxen methyl ester in water-saturated isooctane. It is shown that coupling of the enantioselective hydrolysis of Naproxen methyl ester with the photo-dissociation methanol leads to the photocatalytic conversion of methanol into water, by which the equilibrium constant (K) of the lipase-catalyzed hydrolysis was changed. The equilibrium yield and enantiomeric excess are increased. Because the lipase would not dissolve in the organic solvent, it was adsorbed on photocatalyst particles, which may facilitate the isolation of enzyme from reaction system.     

Determination of monoenoic fatty acid double bond position by permanganate-periodate oxidation followed by high-performance liquid chromatography of carboxylic acid phenacyl esters

This investigation was carried out to develop methods for a reverse-phase, high-performance liquid chromatography analysis of the monocarboxylic and dicarboxylic acids produced by permanganate-periodate oxidation of monoenoic fatty acids. Oxidation reactions were performed using [U-14C]oleic acid and [U-14C]oleic acid methyl ester in order to measure reaction yields and product distributions. The 14C-labeled oxidation products consisted of nearly equal amounts of monocarboxylic and dicarboxylic acid (or dicarboxylic acid monomethyl ester), with few side products (yield greater than 98%). Conversion of the carboxylic acids to phenacyl esters proceeded to completion. HPLC of carboxylic acid phenacyl esters was performed using a C18 column with a linear solvent gradient beginning with acetonitrile/water (1/1) and ending with 100% acetonitrile. Excellent resolution was achieved for all components of a mixture of C5 through C12 monocarboxylic acid phenacyl esters and C6 through C11 dicarboxylic acid phenacyl esters. Resolution was also achieved for all components of a mixture of C5 through C12 monocarboxylic acid phenacyl esters and C6 through C11 dicarboxylic acid monomethyl, monophenacyl esters. The resolution obtained by HPLC demonstrates that, for a wide range of monoenoic fatty acids, both products of a permanganate-periodate oxidation can be identified on a single chromatogram. Free fatty acids and fatty acid methyl esters were analyzed with equal success. Neither the oxidation nor the esterification reaction caused detectable hydrolysis of methyl ester. The method is illustrated for free acids and methyl esters of 14:1 (cis-9), 16:1 (cis-9), 18:1 (cis-6), 18:1 (cis-9), and 18:1 (cis-11).     

Improvement of a process for purification of tocopherols and sterols from soybean oil deodorizer distillate

Soybean oil deodorizer distillate (SODD) is a useful material for purification of tocopherols and phytosterols (referred to as sterols). The SODD was first distilled, and the two substances were enriched. The preparation, which mainly contained free fatty acids (FFAs), sterols, and tocopherols, was named SODD tocopherols/sterols concentrate (SODDTSC). If sterols are converted to steryl esters and FFAs are converted to fatty acid methyl esters (FAMEs), relatively easy purification of tocopherols and steryl esters can be achieved because the boiling points of FAMEs, tocopherols, and steryl esters are different significantly. Hence, the development of a new two-step in situ reaction system was tried out for esterification of sterols with FFAs (first step) and esterification of FFAs with methanol (MeOH) (second step). A mixture of SODDTSC/water (95:5, w/w) and 250 units (U)/g-mixture of Candida rugosa lipase was prepared beforehand for the first-step reaction, and was agitated at 40 °C for 24 h with dehydration at 20 mmHg. Sterols were efficiently esterified, and the degree of esterification reached 95%. To the reaction mixture were added 7 M amounts of MeOH against unreacted FFAs, 20 wt.% water, and 25 U/g-mixture of Alcaligenes sp. lipase. The second-step reaction was then conducted at 30 °C for 20 h. Consequently, 95% FFAs were converted to FAME, and steryl esters synthesized by the first-step reaction were not reconverted to free sterols. Finally, SODDTSC (1.5 kg) was subjected to this two-step in situ reaction, and tocopherols and steryl esters were purified from the reaction mixture by short-path distillation. Tocopherols were purified to 72% (yield, 88%) and steryl esters were purified to 97% (yield, 97%).     

Synthesis of phosphatidylcholine with defined fatty acid in the sn-1 position by lipase-catalyzed esterification and transesterification reaction

The incorporation of caproic acid in the sn-1 position of phosphatidylcholine (PC) catalyzed by lipase from Rhizopus oryzae was investigated in a water activity-controlled organic medium. The reaction was carried out either as esterification or transesterification. A comparison between these two reaction modes was made with regard to product yield, product purity, reaction time, and byproduct formation as a consequence of acyl migration. The yield in the esterification and transesterification reaction was the same under identical conditions. The highest yield (78%) was obtained at a water activity (a(w)) of 0.11 and a caproic acid concentration of 0.8 M. The reaction time was shorter in the esterification reaction than in the transesterification reaction. The difference in reaction time was especially pronounced at low water activities and high fatty acid concentrations. The loss in yield due to acyl migration and consequent enzymatic side reactions was around 16% under a wide range of conditions. The incorporation of a fatty acid in the sn-1 position of PC proved to be thermodynamically much more favorable than the incorporation of a fatty acid in the sn-2 position.     

The chemical and enzymatic oxidation of hematohemin IX. Identification of hematobiliverdin IX alpha as the sole product of the enzymatic oxidation

Oxidative cleavage of hematohemin IX in pyridine solution in the presence of ascorbic acid (coupled oxidation), followed by esterification of the products with boron trifluoride/methanol produced the four possible hematobiliverdin dimethyl esters in 11.1% overall yield. Transetherifications took place simultaneously with the esterification reaction and resulted in the formation of the dimethyl ester of hematobiliverdin IX gamma 8a,13a-dimethyl ether (1.8%), the dimethyl ester of hematobiliverdin IX beta 13a,18a-dimethyl ether (1.9%), the dimethyl ester of hematobiliverdin IX delta 8a-monomethyl ether (1.4%), and the dimethyl ester of hematobiliverdin IX alpha 18a-monomethyl ether (0.4%). The latter was the sole product obtained after the enzymatic oxidation of hematohemin with heme oxygenase, after esterification of the reaction product with boron trifluoride/methanol. When the esterification step was omitted hematobiliverdin IX alpha was obtained from the enzymatic oxidation. The structures of the hematobiliverdin derivatives were secured by their NMR and mass spectra data. Saponification of the dimethyl esters afforded the hematobiliverdin methyl ethers, which were excellent substrates of biliverdin reductase and were readily reduced to the corresponding bilirubins. Hematobiliverdin IX alpha was also a good substrate of biliverdin reductase. It is concluded that the enzymatic oxidation of hematohemin IX by heme oxygenase is alpha-selective, while biliverdin reductase shows no selectivity in the reduction of the four hematobiliverdin isomers.     

Ester synthesis in aqueous media in the presence of various lipases

Summary The ability of seven lipase preparations to catalyse methyl ester synthesis in aqueous media was compared and the synthesis reaction (esterification or alcoholysis) determined. Three behaviours were observed: three enzymes catalysed ester synthesis by esterification of free fatty acids and one enzyme catalysed alcoholysis but the other three lipases did not catalyse a net ester synthesis under the conditions tested. The three groups also differed by the influence of methanol on the hydrolysis reaction. The first group was not significantly inhibited up to the highest methanol concentration tested (5 M). Hydrolysis in the presence of the enzyme of the second group was increasingly inhibited with increasing methanol concentrations. In the presence of the third group, hydrolysis was 40 to 50% inhibited for all the concentrations tested (0.2–5 M).     

Quantitative assessment of methyl‐esterification and other side reactions in a standard propionylation protocol for detection of histone modifications

Histone modifications play an important role in regulating chromatin stability and gene expression, but to date, investigating them remains challenging. In order to obtain peptides suitable for MS‐based analysis, chemical derivatization of N‐terminus and lysine residues by propionic anhydride is commonly performed. Several side reactions (methyl‐esterification, amidation, solvolysis, overpropionylation, and missed propionylation) during propionylation protocols have been described, yet their relative abundances remain vague. Because methyl‐esterification could interfere with correct interpretation of the modification pattern, it is essential to take measures to avoid it. Here we present in‐depth quantitative analyses of methyl‐esterification and the other side reactions in a standard propionylation protocol containing methanol, and when replacing methanol with isopropanol or acetonitrile. We show that the use of alternative solvents can eliminate methyl‐esterification and that even though other side reactions are not prevented, their contribution can be kept relatively small. We also show that replacing methanol can be of importance also in other proteomics methods, such as mixed cation exchange, using methanol under acidic conditions.     

Kinetics of lipase-catalysed methyl gallate production in the presence of deep eutectic solvent

Production of methyl gallate (MG), which is an important phenolic acid ester for pharmaceutical industry, was carried out by Novozym 435-catalysed transesterification of propyl gallate (PG) with methanol in a deep eutectic solvent. Reaction parameters governing substrate molar ratio, enzyme concentration, temperature and agitation rate were investigated batch-wise in choline chloride:glycerol-water binary mixture. The results were evaluated in terms of conversion of PG, yield of MG and hydrolysis of PG to gallic acid. 10% (w/w) of water was found to be favourable in the reaction medium for low hydrolysis percent. The highest conversion (17.4%) and yield (60.4%) but the lowest hydrolysis (2%) after 120?h of transesterification were found at PG/methanol molar ratio of 1:6, enzyme concentration of 40?g/L, 50?°C and 200?rpm. A kinetic model based on the Ping-Pong Bi–Bi mechanism for transesterification of PG was proposed with the assumption that there were no internal and external mass transfer resistances.