Lipase-mediated hydrolysis of corn DDGS oil: Kinetics of linoleic acid production

In this study, we investigated the kinetics of linoleic acid production via lipase-mediated hydrolysis of corn DDGS oil in a batch reactor with continuous mechanical agitation and developed a kinetic model that incorporated the product inhibition to study the complete hydrolysis. The model agreed very well with observed data; though situations with low enzyme dosage or low stirring rates were modeled successfully without product inhibition, actual product concentration in such situations was too low to exert any inhibitory effects. Increasing the enzyme concentration increased hydrolysis, and beyond certain enzyme concentrations, effects tended to fade away because of excessive enzyme desorption from the interface. An enzyme dosage within the range of 40–60 KLU/L of oil dispersion could be successfully applied for a substrate concentration of 25–50 g/L of DDGS oil. Increasing the agitation rates improved enzymatic hydrolysis, but a higher stirring rate of 1000 rpm moderately improved production of linoleic acid compared with a stirring rate of 750 rpm. Within the range of substrate concentrations studied, enzymatic inhibition was moderate but still evident. The high degree of hydrolysis (i.e., ∼96% of theoretical linoleic acid yield) from DDGS oil suggests this method has potential for commercial production of linoleic acid.     

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.     

Optimization and kinetic study on the synthesis of palm oil ester using Lipozyme TL IM

Enzymatic synthesis of palm oil esters (POE) was carried out via alcoholysis of palm oil (PO) and oleyl alcohol (OA) catalyzed by Lipozyme TL IM. The optimum reaction conditions were: temperature: 60 °C; enzyme load: 24.7 wt%; substrate ratio: 1:3 (PO/OA), impeller speed: 275 rpm and reaction time: 3 h. At the optimum condition, the conversion of POE was 79.54%. Reusability study showed that Lipozyme TL IM could be used for 5 cycles with conversion above 50%. The alcoholysis reaction kinetic follows the Ping-Pong Bi-Bi mechanism characterized by the V_max, K_m(PO), and K_m(OA) values of 32.7 mmol/min, 0.3147 mmol/ml and 0.9483 mmol/ml, respectively. The relationship between initial reaction rate and temperature was also established based on the Arrhenius law.     

Optimization of enzymatic hydrolysis of triglycerides in soy deodorized distillate with supercritical carbon dioxide

Enzymatic hydrolysis of triglycerides of soy deodorized distillate (DOD), using immobilized Candida rugosa lipase under supercritical carbon dioxide (SC-CO₂) medium, was carried out. Optimization of the reaction parameters using response surface methodology based on Box-Behnken model at three levels of pressure (120–180 bar), temperature (40–60 °C) and moisture content (40–80% of triglyceride content) for maximum hydrolysis of triglycerides was arrived by multilinear regression of the experimental results. The optimum conditions for maximum degree of triglyceride hydrolysis (94%) were found to be: pressure of 180 bar, temperature of 43 °C and moisture content of 40% to the triglyceride content. Maximum degree of hydrolysis was achieved with short incubation time of 1.5 h under SC-CO₂. Whereas conventional method of hydrolysis in hexane under similar reaction conditions of temperature, moisture and enzyme concentration, needs 5 h to achieve 88% of triglyceride hydrolysis.     

Preparation of a biocatalyst via physical adsorption of lipase from Thermomyces lanuginosus on hydrophobic support to catalyze biolubricant synthesis by esterification reaction in a solvent-free system

Lipase from Thermomyces lanuginosus (TLL) was immobilized on mesoporous hydrophobic poly-methacrylate (PMA) particles via physical adsorption (interfacial activation of the enzyme on the support). The influence of initial protein loading (5–200 mg/g of support) on the catalytic properties of the biocatalysts was determined in the hydrolysis of olive oil emulsion and synthesis of isoamyl oleate (biolubricant) by esterification reaction. Maximum adsorbed protein loading and hydrolytic activity were respectively ≈100 mg/g and ≈650 IU/g using protein loading of 150 mg/g of support. The adsorption process followed the Langmuir isotherm model (R² = 0.9743). Maximum ester conversion around 85% was reached after 30 min of reaction under continuous agitation (200 rpm) using 2500 mM of each reactant in a solvent-free system, 45 °C, 20% m/v of the biocatalyst prepared using 100 mg of protein/g of support. Apparent thermodynamic parameters of the esterification reaction were also determined. Under optimal experimental conditions, reusability tests of the biocatalyst (TLL-PMA) after thirty successive cycles of reaction were performed. TLL-PMA fully retained its initial activity up to twenty two cycles of reaction, followed by a slight decrease around 8.6%. The nature of the product (isoamyl oleate) was confirmed by attenuated total reflection Fourier transform infrared (ATR-FTIR), proton (¹H NMR) and carbon (¹³C NMR) nuclear magnetic resonance spectroscopy analyses.     

Enzymatic synthesis of phenolic lipids in solvent-free medium using flaxseed oil and 3,4-dihydroxyphenyl acetic acid

The enzymatic synthesis of phenolic lipids (PLs) by transesterification of flaxseed oil with 3,4-dihydroxyphenyl acetic acid (DHPA) was investigated in solvent-free medium (SFM), using Novozym 435 from Candida antarctica as the biocatalyst. The effects of selected reaction parameters, water activity (a_w), enzyme concentration and agitation speed, were studied and optimized. Increasing the a_w of the reaction mixture from 0.18 to 0.38 resulted in a significant increase in the bioconversion yield from 62 to 77%. APCI–MS analysis confirmed the formation of six 3,4-dihydroxyphenyl acetoylated lipids, which were monolinolenyl, dioleyl, dilinolenyl, linoleyl linolenyl, oleyl linolenyl and oleyl linoleyl dihydroxyphenyl acetates. The highest enzymatic activity (178 nmol of PLs/g solid enzyme/min) was obtained using 40 mg of solid enzyme (400 PLU)/mL at agitation speed 150 rpm. Using the optimized conditions, the phenolic lipids showed a high relative proportion of linolenic acid (C_18:3 n?3) that increased from 57% in the flaxseed oil to 75 and 64% in the produced phenolic mono- and diacylglycerols, respectively. In addition, the synthesized phenolic lipids demonstrated a 7.2-fold lower radical scavenging activity than that of DHPA but half that of α-tocopherol.     

Optimization of medium chain length fatty acid incorporation into olive oil catalyzed by immobilized Lip2 from Yarrowia lipolytica

Triacylglycerols (TAG) enriched with medium chain fatty acids (M) present specific nutritional, energetic and pharmaceutical properties. Structured lipids (SL) were produced by acidolysis between virgin olive oil and caprylic (C8:0) or capric (C10:0) acids in solvent-free media, catalyzed by the main extracellular lipase from Yarrowia lipolytica lipase 2 (YLL2), immobilized in Accurel MP 1000. Response surface methodology was used for modeling and optimization of the reaction conditions catalyzed by immobilized YLL2. Central composite rotatable designs were performed as a function of the reaction time (2.5–49.5 h) and the molar ratio of medium chain fatty acid/TAG (MR; 0.6–7.4), for both acids, and also of temperature (32–48 ̊C) for C8:0 experiments. As for capric acid, the incorporation of caprylic acid in olive oil showed not to depend of the temperature, within the tested range. The response surfaces, fitted to the experimental data, were described by a first-order polynomial equation, for C8:0 incorporation, and by a second-order polynomial equation for C10:0 incorporation. Under optimized conditions (48 h reaction at 40 ̊C, with a molar ratio of 2:1 M/TAG) the highest incorporation was reached for C8:0 (25.6 mol%) and C10:0 (21.3 mol%).     

Effect of the aeration rate and agitation speed on β-carotene production and morphology of Blakeslea trispora in a stirred tank reactor: mathematical modeling

The effect of aeration rate and agitation speed on β-carotene production and morphology of Blakeslea trispora in a stirred tank reactor was investigated. B. trispora formed hyphae, zygophores and zygospores during the fermentation. The zygospores were the morphological form responsible for β-carotene production. Both aeration and agitation significantly affected β-carotene concentration, productivity, biomass and the volumetric mass transfer coefficient (K_La). The highest β-carotene concentration (1.5 kg m⁻³) and the highest productivity (0.08 kg m⁻³ per day) were obtained at low impeller speed (150 rpm) and high aeration rate (1.5 vvm). Also, maximum productivity (0.08 kg m⁻³ per day) and biomass dry weight (26.4 kg m⁻³) were achieved at high agitation speed (500 rpm) and moderate aeration rate (1.0 vvm). Conversely, the highest value of K_La (0.33 s⁻¹) was observed at high agitation speed (500 rpm) and high aeration rate (1.5 vvm). The experiments were arranged according to a central composite statistical design. Response surface methodology was used to describe the effect of impeller speed and aeration rate on the most important fermentation parameters. In all cases, the fit of the model was found to be good. All fermentation parameters (except biomass concentration) were strongly affected by the interactions among the operation variables. β-Carotene concentration and productivity were significantly influenced by the aeration, agitation, and by the positive or negative quadratic effect of the aeration rate. Biomass concentration was principally related to the aeration rate, agitation speed, and the positive or negative quadratic effect of the impeller speed and aeration rate, respectively. Finally, the volumetric mass transfer coefficient was characterized by the significant effect of the agitation speed, while the aeration rate had a small effect on K_La.     

Production of novel halo-alkali-thermo-stable xylanase by a newly isolated moderately halophilic and alkali-tolerant Gracilibacillus sp. TSCPVG

An aerobic xylanolytic Gracilibacillus sp. TSCPVG growing at moderate to extreme salinity (1–30%) and neutral to alkaline pH (6.5–10.5) was isolated from the salt fields near Sambhar district of Rajasthan, India. β-xylanase (18.44 U/ml) and β-xylosidase (1.01 U/ml) were produced in 60 h in the GSL-2 mineral base medium with additions of (in g/l) Birchwood xylan (7.5), yeast extract (10.0), tryptone (8.0), proline (2.0), thiamine (2.0), Tween-40 (2.0) and NaCl (35) at pH 7.5, 30 °C and 180 rpm. The β-xylanase was active within a broad salinity range (0–30% NaCl), pH (5.0–10.5) and temperature (50–70 °C). It exhibited maximal activity with 3.5% NaCl, pH 7.5 at 60 °C. It was extremely halotolerant retaining more than 80% of activity at 0 and 30% NaCl and alkali-tolerant retaining 76% of activity at pH 10.5. The acetone precipitated xylanase was highly stable (100%) at variable salinities of 0–30% NaCl, pH of 5.0–10.5 and temperatures of 0–60 °C for 48 h. HPLC analysis showed xylose, arabinose and xylooligosaccharides as hydrolysis products of xylan. This is the first report on hemi-cellulose degrading halo-alkali-thermotolerant enzyme from a moderately halophilic Gram-positive Gracilibacillus species.     

Synthesis of structured lipid with balanced omega-3: Omega-6 ratio by lipase-catalyzed acidolysis reaction: Optimization of reaction using response surface methodology

The present study deals with the production of structured lipid containing omega-3 and omega-6 fatty acids in the ratio of 1:1 by incorporating omega-3 fatty acids (α-linolenic acid) from linseed oil into groundnut oil using lipase (Lipozyme IM from Rhizomucor miehei) catalyzed acidolysis reaction in hexane. The reaction conditions were optimized by response surface methodology with a four-variable five-level central composite rotatable experimental design. The influence of four independent parameters, namely ratio of fatty acid concentrate from linseed to groundnut oil (0.66–1.98, w/w), reaction temperature (30–60 °C), enzyme concentration (1–5%) and reaction time (2–54 h) on omega-3 fatty acids incorporation into groundnut oil were optimized. Optimal conditions for the structured lipid containing omega-3 to omega-6 fatty acids in the ratio of 1:1 were determined to be; enzyme concentration 3.75% (w/w), temperature 37.5 °C, incubation time 30.81 h and ratio of free fatty acid concentrate from linseed oil to groundnut oil 1.16 (w/w).     

Exploring a new,soluble lipase for FAMEs production in water-containing systems using crude soybean oil as a feedstock

Performance of a new lipase from Novozymes (Callera Trans L) was studied for fatty acid methylesters (FAMEs) production. In order to reduce the costs of the industrial enzymatic biodiesel production process, the enzyme was used in its soluble form instead of the common immobilized preparations. Cost reduction was also achieved by using crude (non-degummed) soybean oil as a cheaper raw material. The effect of water content during Callera Trans L-catalyzed FAMEs production was explored from evaluation of free fatty acids (FFAs), tri- di or monoacylglycerides (TAGs, DAGs, MAGs) variation during 24 h reaction. An excellent 96% FAMEs release was achieved when low (3–5%) water concentrations were used in the conversion of crude soybean oil. Time course HPLC analysis of the reaction products suggests that the soluble enzyme proceeds through a mechanism of methylester formation based on a first hydrolysis step that releases FFAs, DAGs or MAGs, followed by esterification of FFAs with methanol for FAMEs production.     

Fermentation strategies for the production of lipase by an indigenous isolate Burkholderia sp. C20

Burkholderia sp. C20 strain isolated from food wastes produces a lipase with hydrolytic activities towards olive oil. Fermentation strategies for efficient production of this Burkholderia lipase were developed using a 5-L bench top bioreactor. Critical factors affecting the fermentative lipase production were examined, including pH, aeration rate, agitation rate, and incubation time. Adjusting the aeration rate from 0.5 to 2 vvm gave an increase in the overall lipase productivity from 0.057 to 0.076 U/(ml h), which was further improved to 0.09 U/(ml h) by adjusting the agitation speed to 100 rpm. The production of Burkholderia lipase followed mixed growth-associated kinetics with a yield coefficient of 524 U/g-dry-cell-weight. The pH optimum for cell growth and lipase production was different at 7.0 and 6.0, respectively. Furthermore, stepwise addition of carbon substrate (i.e., olive oil) enhanced lipase production in both flask and bioreactor experiments.     

Biological hydrogen production from CO: Bioreactor performance

This paper presents an alternative solution to the current problem faced by the world; diminishing of fossil fuel. Bioconversion of synthesis gas to hydrogen as clean fuel was catalyzed by a photosynthetic bacterium, Rhodospirillum rubrum. The clean fuel production was biologically mediated by the water–gas shift reaction in a 2 l bioreactor. The work performed was on agitation effects on hydrogen production, K_La and power consumption. The results show that 500 rpm was the suitable agitation rate to be employed. The hydrogen production was optimized at 0.44 ± 0.023 atm giving a K_La of 86.4 ± 3.5 h⁻¹. The production rate was 9.6 mmol H₂/h. The maximum light conversion efficiency at agitation speed of 800 rpm, light intensity of 500 lux (732 kW/m²) and 4 g/l inlet acetate concentration was about 10.84 ± 1.73%. At this condition, the maximum CO conversion efficiency was found to be 81 ± 5.6%. The ratio of power per volume was calculated to be 322.30 ± 12.14 kW/m³ and foaming problem was successfully avoided. The corresponding power consumption was estimated to be about 0.64 ± 0.03 kW, while the output hydrogen energy was determined to be 643.2 ± 26 kW. A prolonged operation of continuous hydrogen production employing a microsparger showed stable behaviour for a duration of 27 days.     

The effect of agitation and aeration on the synthesis and molecular weight of gellan in batch cultures of Sphingomonas paucimobilis

The effects of agitation and aeration upon synthesis and molecular weight of the biopolymer gellan were systematically investigated in batch fermenter cultures of the bacterium, Sphingomonas paucimobilis. High aeration rates and vigorous agitation enhanced growth of S. paucimobilis. Although gellan formation occurred mainly in parallel with cell growth, the increase in cells able to synthesise gellan did not always lead to high gellan production. For example, at very high agitation rates (1000 rpm) growth was stimulated at the expense of biopolymer synthesis.Maximal gellan concentration was obtained at 500 rpm agitation and either 1 or 2 vvm aeration (12.3 and 12.4 g/l gellan, respectively). An increase in aeration (from 1 to 2 vvm) enhanced gellan synthesis only at low agitation rates (250 rpm). However, high aeration or dissolved oxygen was not necessary for high gellan synthesis, in fact oxygen limitation always preceded the phase of maximum gellan production and probably enhanced polysaccharide biosynthesis.Some gellan was formed even after glucose exhaustion. This was attributed to the intracellular accumulation of polyhydroxyalkanoates, (such as polyxydroxybutyrate) which were found in S. paucimobilis cells indicating the existence of a carbon storage system, which may contribute to gellan biosynthesis under glucose-limiting conditions.The autolysis of the culture, which occurred at the late stages of the process, seemed to be triggered mainly by limitations in mass (nutrient) transfer, due to the highly viscous process fluid that gradually develops. Rheological measurements generally gave a very good near real time estimate of maximum biopolymer concentration offering the possibility of improved process control relative to time consuming gravimetric assay methods.While mechanical depolymerisation of gellan did not occur, high aeration rates (2 vvm) led to production of gellan of low molecular weight (at either 250 or 500 rpm). This effect of aeration rate upon gellan molecular weight is reported here for the first time, and is important for the properties and applications of gellan. Mechanisms which may have led to this are discussed, but control of molecular weight of the biopolymers is clearly an area needing further research.     

Optimization of the aeration and agitation speed of Aeribacillus palidus 418 exopolysaccharide production and the emulsifying properties of the product

The specific properties of exopolysaccharides (EPS) from thermophilic microorganisms have attracted interest in their optimized production. In this study, the ability of Aeribacillus pallidus 418 to grow and produce polysaccharide in a 5-l stirred tank bioreactor was investigated. Agitation rates of 100, 200, 600, 900, and 1100 revolutions per minute (rpm), at an air flow rate of 0.5 gas volumes per unit medium volume per minute (vvm), and aeration rates of 0.25, 0.5, 1.0, and 1.5 vvm, at an agitation rate of 900 rpm, were examined. A maximum EPS yield of 170 μg/ml has been registered in a single impeller bioreactor equipped with an original Narcissus impeller at agitation speed of 900 rpm, with an aeration rate of 0.5 vvm. The bioprocess oxygen uptake rate (OUR) and oxygen mass transfer coefficient (K_La) were evaluated. The emulsifying properties of the specific EPS produced by A. pallidus 418 were determined. Stable oil-in-water emulsions, a low level of separated water phase and high dispersion stability were found, which together demonstrate the prospects for the industrial exploration of EPS production. Enhanced synergism between the A. pallidus 418 synthesized EPS and various commercially used hydrocolloids was observed; superior synergy was achieved in combination with xanthan gum.     

Agitation,aeration and shear stress as key factors in inulinase production by Kluyveromyces marxianus

Factorial design and response surface analyses were used to optimize the production of inulinase (2,1-β-d-fructan fructanohydrolase, EC 3.2.1.7) by Kluyveromyces marxianus ATCC 16045, using sucrose as carbon source. Effects of aeration, agitation and type of impeller (disk turbine, marine, pitched blade) were studied in a batch stirred reactor. Two factorial designs 2² were carried out. Agitation speed varied from 50 to 550 rpm (revolution per minute), aeration rate from 0.5 to 2.0 vvm (air volume/broth volume·minute). It has been shown that the enzyme production was strongly influenced by mixing conditions, while aeration rate was shown to be less significant. Additionally, the increase in the agitation speed is limited by the death rate, which increases drastically at high speeds, lowering the enzyme production. Also, the impeller type has significant influence in the production, the disk impeller at 450 rpm and aeration at 1.0 vvm led to an activity of 121 UI/mL, while the pitched blade was shown to be the best impeller for this process, leading to the best production, 176 UI/mL, at 450 rpm and 1.0 vvm. The maximum shear stress for inulinase production was about 0.22 Pa, since higher values cause higher cell death rates, affecting the enzyme production. The same results were confirmed with another microorganism, which was also sensible to shear stress. Therefore, it has been concluded that in some cases, mainly when the microorganism is sensible to shear stress, the interaction between mass transfer and mechanical stress should be considered in scale up processes.     

Effects of pellet morphology on broth rheology in fermentations of Aspergillus terreus

Effects of pellet morphology on broth rheology are reported for pelleted submerged cultures of the lovastatin producing filamentous fungus Aspergillus terreus, growing in fluidized bed and stirred tank bioreactors. The pellet diameter and compactness were affected by the agitation intensity of the broth; however, the total biomass productivity was not affected. In fluidized beds and stirred tanks with agitation intensity of up to 300 rpm (impeller tip speed of 1.02 m s⁻¹), the fungal pellets were stable at diameters of up to about 2300 μm. In more intensely agitated stirred tanks (≥600 rpm; impeller tip speed of ≥2.03 m s⁻¹), the stable pellet size was only about ≤900 μm. The biomass concentration and the pellet diameter were the main factors that influenced the flow index and the consistency index of the power-law broths. Because the biomass productivity was the same in all experiments in a given type of reactor and the oxygen concentration was kept at ∼400% of air saturation, the pellet size and morphology were not influenced by oxygen mass transfer effects. Pellets were always dense in the core region and no necrosis of the biomass occurred.     

Enzymatic purification of dihomo-γ-linolenic acid from Mortierella single-cell oil

Purification of dihomo-γ-linolenic acid (20:3n−6; DGLA) from a single-cell oil containing 39 wt.% DGLA was attempted. The process comprised: (i) non-selective hydrolysis of the oil to prepare a mixture of free fatty acids (FFAs); (ii) urea adduct fractionation of the FFA mixture to remove saturated fatty acids; and (iii) repeated selective esterification of the resulting mixture with two kinds of lipases. In the first step, Candida rugosa lipase (Lipase-OF from Meito Sangyo Co. Ltd., Aichi, Japan) was the most effective for preparation of the FFAs from the oil; 99% hydrolysis was achieved by the reaction at 40 °C for 72 h. Urea adduct fractionation of the FFA mixture removed almost completely behenic and lignoceric acids, and the content of DGLA increased from 39 to 55 wt.%. The FFAs were esterified with 2 mol equivalent of lauryl alcohol (LauOH) using C. rugosa lipase (Lipase-AY from Amano Enzyme Inc., Aichi, Japan). In consequent, DGLA was enriched to 86 wt.% in the unesterified FFA fraction. To further increase the content of DGLA, the esterification was repeated using the same lipase. Accordingly, the content of DGLA increased to 91 wt.%, but the preparation was contaminated with 3.3 wt.% γ-linolenic acid. This contaminant was removed finally by selective esterification of the FFAs with 2 mol equivalent of LauOH using Pseudomonas aeruginosa lipase. A series of procedures purified DGLA to 95 wt.% in a yield of 51% of the initial content in the single-cell oil.     

Ultrasonic irradiation with vibration for biodiesel production from soybean oil by Novozym 435

The production of biodiesel with soybean oil and methanol through transesterification by Novozym 435 (Candida antarctica lipase B immobilized on polyacrylic resin) were conducted under two different conditions—ultrasonic irradiation and vibration to compare their overall effects. Compared with vibration, ultrasonic irradiation significantly enhanced the activity of Novozym 435. The reaction rate was further increased under the condition of ultrasonic irradiation with vibration (UIV). Effects of reaction conditions, such as ultrasonic power, water content, organic solvents, ratio of solvent/oil, ratio of methanol/oil, enzyme dosage and temperature on the activity of Novozym 435 were investigated under UIV. Under the optimum conditions (50% of ultrasonic power, 50 rpm vibration, water content of 0.5%, tert-amyl alcohol/oil volume ratio of 1:1, methanol/oil molar ratio of 6:1, 6% Novozym 435 and 40 °C), 96% yield of fatty acid methyl ester (FAME) could be achieved in 4 h. Furthermore, repeated use of Novozym 435 after five cycles showed no obvious loss in enzyme activity, which suggested this enzyme was stable under the UIV condition. These results indicated that UIV was a fast and efficient method for biodiesel production.