Chemometric analysis of lipase-catalyzed synthesis of xylitol esters in a solvent-free system

Immobilized Candida antarctica lipase B-catalyzed esterification of xylitol and two fatty acids (capric and caproic acid) were studied in a solvent-free system. The Taguchi orthogonal array method based on three-level-four-variables with nine experiments was applied for the analysis and optimization of the reaction parameters including time, substrate molar ratio, amount of enzyme, and amount of molecular sieve. The obtained conversion was higher in the esterification of xylitol and capric acid with longer chain length. The optimum conditions derived via the Taguchi approach for the synthesis of xylitol caprate and xylitol caproate were reaction time, 29 and 18 h; substrate molar ratio, 0.3 and 1.0; enzyme amount, 0.20 and 0.05 g, and molecular sieve amount of 0.03 g, respectively. The good correlation between the predicted conversions (74.18% and 61.23%) and the actual values (74.05% and 60.5%) shows that the model derived from the Taguchi orthogonal array can be used for optimization and better understanding of the effect of reaction parameters on the enzymatic synthesis of xylitol esters in a solvent-free system.     

Effect of Solvents and Kinetic Parameters on Synthesis of Ethyl Propionate Catalysed by Poly (AAc-co-HPMA-cl-MBAm)-Matrix-Immobilized Lipase of Pseudomonas aeruginosa BTS-2.

Summary A purified alkaline thermo-tolerant bacterial lipase from Pseudomonas aeruginosa BTS-2 was immobilized on a poly (AAc-co-HPMA-cl-MBAm) hydrogel network. The hydrogel showed approximately 95% binding efficiency for lipase (specific activity 1.96 U mg⁻¹). The immobilized enzyme achieved 65.1% conversion of ethanol and propionic acid (100 mM each) into ethyl propionate in n-nonane at 65 °C in 9 h. When alkane of C-chain length lower than n-nonane was used as the organic solvent, the conversion of ethanol and propionic acid into ethyl propionate decreased with a decrease in the log P value of alkanes. The immobilized lipase retained approximately 30% of its original catalytic activity after five cycles of reuse for esterification of ethanol and propionic acid into ethyl propionate at temperature 65 °C in 3 h. Addition of a molecular sieve (3 ?) to the reaction mixture enhanced the formation of ethyl propionate to 89.3%. Moreover, ethanol and propionic acid when taken a molar ratio of 3:1 further promoted the conversion rate to 94%. However, an increase in the molar ratio of propionic acid with respect to ethanol resulted in a decline of ethyl propionate synthesis.     

Continuous enzymatic esterification of glycerol with (poly)unsaturated fatty acids in a packed-bed reactor

Enzymatic synthesis of mono-, di-, and triacyglycerols from (poly)unsaturated fatty acids (linoleic, oleic, and conjugated linoleic acids) has been studied as a solvent-free reaction in a packed-bed reactor containing an immobilized lipase from Mucor miehei. The extents of the esterification reactions of interest are primarily determined by the molar ratio of glycerol to fatty acid because the presence of excess glycerol as a immiscible phase is responsible for reducing the activity of the water produced by the esterification reactions. For molar ratios of fatty acid to glycerol of less than 1.5, the percentage of the fatty acid esterified decreases quasi-linearly with an increase in this molar ratio. By appropriate manipulation of the fluid-residence time, one can control the relative proportions of the various acylglycerols in the effluent stream. At the outlet of the reactor, one observes excellent spontaneous separation of the glycerol and acylglycerol/fatty acid phases. At 50 degrees C and a fluid residence time of 1 hour, as much as 90% of the fatty acid can be esterified when the molar ratio of fatty acid to glycerol is 0.33 or less.     

填充床反应器中酶法连续合成甘油二酯的研究

近年来,1,3-甘油二酯(DAG)由于其广泛用途及健康作用日益受到人们的重视。报道了一种无溶剂条件下填充床反应器中连续酶促合成1,3-DAG的方法。研究了填充柱的长径比、进料体积流速、温度、底物摩尔比对酯化率和1,3-DAG产量的影响。结果表明固定化酶填充柱长径比7.8,亚油酸、甘油摩尔比1∶2 ,进料速度1.2mL/min ,65℃条件下酯化反应可实现脂肪酸酯化率、1,3-DAG纯度及生产效率的统一。填充床反应器中固定化酶连续催化酯化反应的一个主要问题即体系水分清除困难。实验研究了采用过量甘油吸附脱水的可行性,亚油酸、甘油摩尔比为1∶2时,可明显改善固定化酶的稳定性,增加LipozymeRMIM的使用寿命。连续运行10d ,残余酶活仍保持在80 %以上,而对照组则仅为52%。     

基于响应面设计脂肪酶Novo435催化合成甘油二酯的工艺优化

以甘油、油酸为原料,优化在无溶剂体系中以固定化脂肪酶Novo435催化合成甘油二酯（diglyceride,DAG）的工艺。系统考察底物摩尔比（油酸／甘油）、反应温度、时间和加酶量等因素对油酸转化率和甘油二酯含量影响的基础上,利用响应面试验设计优化各主效因子,并经回归分析获得最优的工艺条件。所得最优条件：油酸与甘油底物摩尔比2．27、反应温度48．14℃、反应时间6．3h、加酶量1．68％。在此条件下,实验测得油酸转化率为45．42％,甘油二酯质量分数为70．01％,与响应面模型预测值吻合。     

Acetylation of glycerol to biofuel additives over sulfated activated carbon catalyst

Oxygenated fuel additives can be produced by acetylation of glycerol. A 91% glycerol conversion with a selectivity of 38%, 28% and 34% for mono-, di- and triacetyl glyceride, respectively, was achieved at 120 °C and 3 h of reaction time in the presence of a catalyst derived from activated carbon (AC) treated with sulfuric acid at 85 °C for 4h to introduce acidic functionalities to its surface. The unique catalytic activity of the catalyst, AC-SA5, was attributed to the presence of sulfur containing functional groups on the AC surface, which enhanced the surface interaction between the glycerol molecule and acyl group of the acetic acid. The catalyst was reused in up to four consecutive batch runs and no significant decline of its initial activity was observed. The conversion and selectivity variation during the acetylation is attributed to the reaction time, reaction temperature, catalyst loading and glycerol to acetic acid molar ratio.     

Biosynthesis of glycerol carbonate from glycerol by lipase in dimethyl carbonate as the solvent

Glycerol carbonate was synthesized from renewable glycerol and dimethyl carbonate using lipase in solvent-free reaction system in which excess dimethyl carbonate played as the reaction medium. A variety of lipases have been tested for their abilities to catalyze transesterification reaction, and Candida antartica lipase B and Novozyme 435 exhibited higher catalytic activities. The silica-coated glycerol with a 1:1 ratio was supplied to prevent two-phase formation between hydrophobic dimethyl carbonate and hydrophilic glycerol. Glycerol carbonate was successfully synthesized with more than 90% conversion from dimethyl carbonate and glycerol with a molar ratio of 10 using Novozyme 435-catalyzed transesterification at 70 °C. The Novozyme 435 [5% (w/w) and 20% (w/w)] and silica gel were more than four times recycled with good stability in a repeated batch operation for the solvent-free synthesis of glycerol carbonate.     

Production of glycerides from glycerol and fatty acid by immobilized lipases in non-aqueous media

Immobilized Mucor miehei lipase catalyzes synthesis reactions between glycerol and oleic acid. No organic solvent is necessary to solubilize the substrates, which allows for the use of a reaction medium solely composed of the necessary substrates. Water produced in the reaction evaporates due to the high temperature used for the process. A conversion of 86% of oleic acid into triolein is obtained when using the substrates in stoichiometric amounts. Varying the ratio of glycerol over oleic acid allows for the preferential synthesis of one of the glycerides. Some batch reactors have been set up using different means of removing the water: spontaneous evaporation, molecular sieves, vacuum, and dry air bubbling.     

β-galactosidase-catalyzed synthesis of 3-O-β-D-galactopyranosyl-sn-glycerol: Optimization by response surface methodology

In this study, the synthesis of 3-O-β-D-galactopyranosyl-sn-glycerol (GG) was performed by the reverse hydrolysis of D-galactose and glycerol using β-galactosidase from Kluyveromyces lactis. Four process variables, reaction temperature (30.0–45.0?°C), reaction time (24–48?h), enzyme concentration (150.00–350.00?U/mL), and substrate molar ratio (glycerol:D-galactose, 7.5:12.5?mmol/mmol) were investigated and optimized via response surface methodology (RSM) for optimal GG synthesis. Both quadratic equations and the optimal reaction conditions were established. Results showed that the four variables, i.e., reaction temperature, reaction time, enzyme concentration, and substrate molar ratio had significant (p?β-galactosidase concentration and 8.65:1.00 of substrate molar concentration ratio (glycerol: D-galactose) at 39.8?°C and 48?h of reaction. Under these conditions, the GG concentration was 140.03?g/L and GG yield was 55.71%, which both were close to the predicted values (143.26?g/L and 56.73%). This finding proves the RSM to be a useful tool in optimizing process conditions for GG synthesis.     

Kinetic characterisation of enzymatic esterification in a solvent system: adsorptive control of water with molecular sieves

The kinetics of enzymatic esterification of glycerol with oleic acid, in equimolar ratio, catalyzed by immobilized Mucor miehei lipase in a solvent system in the presence of the molecular sieves was carried out at 37°C at different Lipozym and solvent (n-hexane) concentrations and the molecular sieve contents were studied in a batch stirred-tank reactor (BSTR). The reactions were followed by the determination of reaction conversions during 45 h. The experimental data of enzymatic esterification of glycerol with oleic acid in a solvent system in the presence of molecular sieves showed minimal deviation from the calculated value in the irreversible second order kinetic model. On the basis of the experimental data, we found an empirical correlation between concentrations of Lipozym, concentrations of solvent (n-hexane), contents of the molecular sieve and the reaction rate constant, k₁.     

Biodiesel production using Aspergillus niger as a whole‐cell biocatalyst in a packed‐bed reactor

Enzymatic lipase transesterification of palm oil to biodiesel in a packed‐bed reactor (PBR) using a novel strain of the fungus Aspergillus niger, immobilized within polyurethane biomass support particles (BSPs), was investigated. A three‐step addition of methanol was used to reduce lipase inhibition by immiscible methanol. The influence of water content and PBR flow rate was investigated. FAME yield was enhanced with an increase of PBR flow rate in the range of 0.15–30 L h^?1, where inefficient mixing of the reaction mixture at lower flow rates resulted in low conversion rates i.e. 69% after 72‐h reaction. Adding the third mole equivalent of methanol resulted in lipase inhibition due to methanol migration into the accumulated glycerol layer. Glutaraldehyde (GA) solution (0.5 vol.%) was used to stabilize lipase activity, which led to a high FAME yield (>90%) in the PBR after 72‐h of reaction time at a flow rate of 15 L h^?1, and a water content of 15%. Moreover, a high conversion rate (>85%) was maintained after four palm oil batch conversion cycles in the PBR. In contrast, lipase activity of non‐GA‐treated cells decreased with each PBR batch cycle, where only 70% FAME was produced after the forth PBR cycle. Transesterification of palm oil in a PBR system using BSPs‐immobilized A. niger as a whole‐cell biocatalyst is a viable process for enzymatic biodiesel production.     

Synthesis of monoacylglycerol containing pinolenic acid via stepwise esterification using a cold active lipase

High purity monoacylglycerol (MAG) containing pinolenic acid was synthesized via stepwise esterification of glycerol and fatty acids from pine nut oil using a cold active lipase from Penicillium camembertii as a biocatalyst. Effects of temperature, molar ratio, water content, enzyme loading, and vacuum on the synthesis of MAG by lipase‐catalyzed esterification of glycerol and fatty acid from pine nut oil were investigated. Diacylglycerol (DAG) as well as MAG increased significantly when temperature was increased from 20 to 40°C. At a molar ratio of 1:1, MAG content decreased because of the significant increase in DAG content. Water has a profound influence on both MAG and DAG content through the entire course of reaction. The reaction rate increased significantly as enzyme loading increased up to 600 units. Vacuum was an effective method to reduce DAG content. The optimum temperature, molar ratio, water content, enzyme loading, vacuum, and reaction time were 20°C, 1:5 (fatty acid to glycerol), 2%, 600 units, 5 torr, and 24 h, respectively. MAG content further increased via lipase‐catalyzed second step esterification at subzero temperature. P. camembertii lipase exhibited esterification activity up to ?30°C. © 2012 American Institute of Chemical Engineers Biotechnol. Prog., 2012     

A practical approach to obtain high yield lipase-mediated synthesis of octyl caprylate with Novozym 435

Abstract

This study evaluated coupled effects of molar ratio of substrates and enzyme loading in a solvent-free system using a simple mathematical approach to obtain high conversions on octyl caprylate synthesis with Novozym 435. When molar ratios of caprylic acid to n-octanol (1:1 and 1:3) were evaluated with enzyme loadings of 1% to 4% (wt/wt acid), an interdependence between the masses of reagents and the enzymes was observed, that was expressed as a mathematical relation. The study of this relation, named as SER, indicated a specific range of reaction conditions that resulted in conversions above 90%. The most suitable condition corresponded to an acid:alcohol molar ratio of 1:1.3 and an enzyme loading of 1.5%, resulting in 94.5% of conversion at 65?°C in 3?hours of reaction. A different reaction system (bottle reactor) was used to evaluate the influence of reagents mixture and heat distribution. The use of a bottle reactor allowed yield improvement that reached 99.3%. At this condition, Novozym 435 was reused, without washing steps, in three subsequent batches keeping high conversion. A possible balance between the shift of chemical equilibrium by stoichiometric excess of reagents and enzymatic inhibition effects by substrates can be expressed mathematically in a convenient way, helping to predict the behaviour of synthesis in different conditions. The mathematical relation proposed, SER, allowed the achievement of 99% of conversion on enzymatic synthesis of octyl caprylate.     

Lipase-catalyzed synthesis of monoacylglycerol in a homogeneous system

The 1,3-regiospecifique lipase, Lipozyme IM, catalyzed the esterification of lauric acid and glycerol in a homogeneous system. To overcome the drawback of the insolubility of glycerol in hexane, which is extensively used in enzymatic synthesis, a mixture of n-hexane/tert-butanol (1:1, v/v) was used leading to a monophasic system. The conversion of lauric acid into monolaurin was 65% in 8 h, when a molar ratio of glycerol to fatty acid (5:1) was used with the fatty acid at 0.1 M, and the phenomenon of acyl migration was minimized.     

Biocatalytic acylation of sugar alcohols by 3-(4-hydroxyphenyl)propionic acid

Enzymatic synthesis of aromatic esters of four different sugar alcohols (xylitol, arabitol, mannitol, and sorbitol) with 3-(4-hydroxyphenyl)propionic acid was performed in organic solvent medium, using immobilized Candida antarctica lipase (Novozyme 435), and molecular sieves for control of the water content. The influence of reaction parameters on the conversion has been investigated, including reaction time, temperature, alcohol/acid molar ratio, and enzyme amount. The highest conversions (94% for xylitol, 98% for arabitol, 80% for mannitol, and 93% for sorbitol) were obtained in pure tert-butanol at 60 °C and 72 h reaction time, 0.3 alcohol/acid molar ratio, and 0.5 g/mol enzyme/substrate ratio. The isolated new sugar alcohols esters were identified by different spectral analyses. MALDI-TOF MS analysis showed the formation of monoesters, diesters, and small quantities of triesters for all investigated sugar alcohols. The catalytic efficiency of the enzyme was higher for the pentitol substrates, decreasing in the following order: arabitol > xylitol > sorbitol > mannitol. These new compounds could have interesting applications in food, pharmaceutical and cosmetic formulations.     

非水相酶促合成癸酸偏甘油酯的研究

对无溶剂非水相中癸酸与甘油的酶促酯化反应进行了研究,发现Pseudomonas fluoresces脂肪酶（PFL）、Mucor miehei脂肪酶（MML）和Candida antarictica脂肪酶（CAL）均有较好的催化活性。CAL酶促转化癸酸的最适反应条件为：60℃,加酶量为20～100u/g,初始加水量为甘油质量的12%。CAL的1,3位置专一性在最终产物中未表达。CAL酶催化剂的失活主要与机械磨损有关,反应5批次后酶活残留量为96.4%。敞开物系、真空脱水或分子筛脱水均为有效脱水方式。敞开物系中反应物量比不影响平衡转化率而会影响单甘酯平衡产率。用碳酸氢钠水溶液萃取可有效脱除产品中的残余癸酸,终产品酸价为0.68mg KOH/g。提高甘油比例并使用非脱水原料,无外加水结合部分流加癸酸的工艺,可以减少减压脱水或敞开反应的时间,5h后癸酸最高转化率可达96.9%。      

Prediction of the equilibrium conversion for the synthesis of acyl hexose through lipase-catalyzed condensation in water-miscible solvent in the presence of molecular sieve

A method is proposed for predicting the equilibrium conversion for the synthesis of monoacyl hexose through the lipase-catalyzed condensation of a fatty acid and a hexose in a water-miscible solvent in the presence of a molecular sieve, based on the apparent reaction equilibrium constant, the adsorption isotherm of water on the molecular sieve, the solubility of hexose in the solvent, and the mass balance with respect of water. Validity of the model was examined for the syntheses of lauroyl mannose, lauroyl glucose, and myristoyl mannose in acetonitrile, 2-methyl-2-propanol, or 2-methyl-2-butanol with molecular sieves 3A 1/16 and 4A 1/16. The predicted conversions agreed well with the experimental values except for the case where a significant amount of diester was formed as the result of the addition of an excess amount of the molecular sieve to the solvent or the high molar ratio of the fatty acid to the hexose.     

Optimization of enzymatic biodiesel synthesis using RSM in high pressure carbon dioxide and its scale up

Enzymatic synthesis of biodiesel by the transesterification of canola oil and methanol in high pressure carbon dioxide [HPCO₂: near-critical and supercritical carbon dioxide (NcCO₂ and ScCO₂)] was optimized using response surface methodology (RSM). RSM based on 5-level-5-factor central composite rotatable design (CCRD) was used to evaluate the effects of temperature, pressure, enzyme loading, substrate molar ratio, and time on the conversion to biodiesel by transesterification. Finally, batch reactions for biodiesel synthesis were preformed in a 100 mL and 7 L high-pressure stirred batch reactors.     

Optimisation of n-octyl oleate enzymatic synthesis over Rhizomucor miehei lipase

Octyl oleate is a useful organic compound with several applications in cosmetic, lubricant and pharmaceutical industry. At first, the enzymatic synthesis of n-octyl oleate by direct lipase-catalysed esterification of oleic acid and 1-octanol was investigated in a stirred batch reactor in solvent-free system. A systematic screening and optimisation of the reaction parameters were performed to gain insight into the kinetics mechanism. Particularly, enzyme concentration, reaction temperature, stirrer speed, water content, substrates concentration and molar ratio were optimised with respect to the final product concentration and reaction rate. The kinetics mechanism of the reaction was investigated. Finally, a comparison of the experimental results obtained in a solvent free-system with those using two different solvents, supercritical carbon dioxide (SC-CO₂) and n-hexane, was proposed. It resulted that in SC-CO₂ higher concentration of the desired product was attained, requiring lower enzyme concentrations to achieve comparable conversion of free fatty acid into fatty acid ester.     

Synthesisof fructose laurate esters catalyzed by a CALB-displaying Pichia pastoris whole-cell biocatalyst in a non-aqueous system

Earlier studies on fructose laurate ester products have shown that recombinant Pichia pastoris displaying Candida antarctica lipase B (CALB) on the cell surface acts as an efficient whole-cell biocatalyst for sugar ester production from fructose and lauric acid in an organic solvent. The effects of various reaction factors, including solvent composition, substrate molar ratio, enzyme dose, temperature and water activity, on esterification catalyzed by the CALB-displaying P. pastoris whole-cell biocatalyst were examined in the present study. Under the preferred reaction conditions, specifically, 5 mL organic solvent mixture of 2-methyl-2-butanol/DMSO (20% v/v), 2 mmol fructose with a lauric acid to fructose molar ratio of 2:1, 0.3 g whole-cell biocatalyst (1,264 U/g dry cell) with an initial water activity of 0.11, 1.2 g 4Å molecular sieve, reaction temperature of 55oC and 200 rpm stirring speed, the fructose mono laurate ester yield was 78% (w/w). The CALBdisplaying P. pastoris whole-cell biocatalyst exhibited good operational stability, with an evident increase, rather than decrease, in relative activity after the continuous recover and reuse cycle. The relative activity of the biocatalyst remained 50% higher than that of the first batch, even following reuse for 15 batches. Our results collectively indicate that the CALB-displaying P. pastoris whole-cell biocatalyst may be potentially utilized in lieu of free or immobilized enzyme to effectively produce non-ionic surfactants such as fatty acid sugar esters, offering the significant advantages of cost-effectiveness, good operational stability and mild reaction conditions.