Microwave-assisted enzymatic synthesis of beef tallow biodiesel

Optimal conditions for the microwave-assisted enzymatic synthesis of biodiesel have been developed by a full 2² factorial design leading to a set of seven runs with different combinations of molar ratio and temperature. The main goal was to reduce the reaction time preliminarily established by a process of conventional heating. Reactions yielding biodiesel, in which beef tallow and ethanol used as raw materials were catalyzed by lipase from Burkholderia cepacia immobilized on silica-PVA and microwave irradiations within the range of 8–15 W were performed to reach the reaction temperature. Under optimized conditions (1:6 molar ratio of beef tallow to ethanol molar ratio at 50°C) almost total conversion of the fatty acid presented in the original beef tallow was converted into ethyl esters in a reaction that required 8 h, i.e., a productivity of about 92 mg ethyl esters g⁻¹ h⁻¹. This represents an increase of sixfold for the process carried out under conventional heating. In general, the process promises low energy demand and higher biodiesel productivity. The microwave assistance speeds up the enzyme catalyzed reactions, decreases the destructive effects on the enzyme of the operational conditions such as, higher temperature, stability, and specificity to its substrate, and allows the entire reaction medium to be heated uniformly.     

Screening Botryosphaeria species for lipases: Production of lipase by Botryosphaeria ribis EC-01 grown on soybean oil and other carbon sources

Nine isolates of Botryosphaeria spp. were screened for lipases when cultivated on eight different plant seed oils and glycerol, and all produced lipases. Botryosphaeria ribis EC-01 produced highest lipase titres on soybean oil and glycerol, while eight isolates of Botryosphaeria rhodina produced significantly lower enzyme titres. B. ribis EC-01 produced lipase when grown on different fatty acids, surfactants, carbohydrates and triacylglycerols, with highest enzyme titres produced on Triton X-100-emulsified stearic (316.7 U/mL), palmitic (283.5 U/mL) and oleic (247.4 U/mg) acids, and soybean oil (105.6 U/mL), as well as castor oil (191.2 U/mg); an enhancement of 9-fold over soybean oil-grown cultures. Glycerol was also a good substrate for lipase production. The crude lipase extract was optimally active at pH 8.0 and 55 °C, stable between 30 and 55 °C and pH 1–10, and tolerant to 50% (v/v) glycerol, methanol and ethanol. The crude lipase showed affinity for substrates of short, average and long-chain fatty acids (different esters of p-nitrophenol and triacylglycerols). Zymograms developed with 4-methylumbelliferyl-butyrate showed two bands of lipolytic activity at 45 and 15 kDa. This is the first report on the production of lipases by B. ribis grown on these different carbon sources.     

Production of biodiesel by Burkholderia cepacia lipase as a function of process parameters

Despite the already established route of chemically catalyzed transesterification reaction in biodiesel production, due to some of its shortcomings, biocatalysts such as lipases present a vital alternative. Namely, it was noticed that one of the key shortcomings for the optimization of the enzyme catalyzed biodiesel synthesis process is the information on the lipase activity in the reaction mixture. In addition to making optimization difficult, it also makes it impossible to compare the results of the independent research. This article shows how lipase intended for use in biodiesel synthesis can be easily and accurately characterized and what is the enzyme concentration that enables achievement of the desired level of fatty acid methyl esters (FAME) in the final product mixture. Therefore, this study investigated the effect of two different activity loads of Burkholderia cepacia lipase on the biodiesel synthesis varying the pH and temperature optimal for lipase activity. The optimal lipase pH and temperature were determined by two different enzyme assays: spectrophotometric and titrimetric. The B. cepacia lipase pH optimum differentiated between assays, while the lipase optimally hydrolyzed substrates at 50°C. The analysis of FAME during 24 hr of biodiesel synthesis, at two different enzyme concentrations, pH 7, 8, and 10, and using two different buffers, revealed that the transesterification reaction at optimal pH, 1 hr reaction time and lipase activity load of 250 U per gram of reaction mixture was sufficient to produce more than 99% FAME.     

Continuous lipase-catalyzed production of fatty acid ethyl esters from soybean oil in compressed fluids

This work investigates the continuous production of fatty acid ethyl esters from soybean oil in compressed fluids, namely carbon dioxide, propane and n-butane, using immobilized Novozym 435 as catalyst. The experiments were performed in a packed-bed bioreactor evaluating the effects of temperature in the range of 30–70 °C, from 50 to 150 bar, oil to ethanol molar ratio of 1:6–1:18 and solvent to substrates mass ratio of 4:1–10:1. In contrast to the use of carbon dioxide and n-butane, results showed that lipase-catalyzed alcoholysis in a continuous tubular reactor in compressed propane might be a potential route to biodiesel production as high reaction conversions were achieved at mild temperature (70 °C) and pressure (60 bar) conditions in short reaction times.     

Combination of two lipases more efficiently catalyzes methanolysis of soybean oil for biodiesel production in aqueous medium

A combination of two lipases was employed to catalyze methanolysis of soybean oil in aqueous medium for biodiesel production. The two lipase genes were cloned from fungal strains Rhizomucor miehei and Penicillium cyclopium, and each expressed successfully in Pichia pastoris. Activities of the 1,3-specific lipase from R. miehei (termed RML) and the non-specific mono- and diacylglycerol lipase from P. cyclopium (termed MDL) were 550 U and 1545 U per ml respectively, and enzymatic properties of these supernatant of fermentation broth (liquid lipase) were stable at 4 °C for >3 months. Under optimized conditions, the ratio of biodiesel conversion after 12 h at 30 °C, using RML alone, was 68.5%. When RML was assisted by addition of MDL, biodiesel conversion ratio was increased to >95% under the same reaction conditions. The results suggested that combination of lipases with different specificity, for enzymatic conversion of more complex lipid substrates, is a potentially useful strategy for biodiesel production.     

Lipase-catalyzed transesterification of soybean oil for biodiesel production in <Emphasis Type="Italic">tert</Emphasis>-amyl alcohol

Lipase-catalyzed transesterification of soybean oil and methanol for biodiesel production in tert-amyl alcohol was investigated. The effects of different organic medium, molar ratio of substrate, reaction temperature, agitation speed, lipase dosage and water content on the total conversion were systematically analyzed. Under the optimal conditions identified (6 mL tert-amyl alcohol, three molar ratio of methanol to oil, 2% Novozym 435 lipase based on the soybean oil weight, temperature 40°C, 2% water content based on soybean oil weight, 150 rpm and 15 h), the highest biodiesel conversion yield of 97% was obtained. With tert-amyl alcohol as the reaction medium, the negative effects caused by excessive molar ratio of methanol to oil and the by-product glycerol could be reduced. Furthermore, there was no evident loss in the lipase activity even after being repeatedly used for more than 150 runs.     

Synthesis of lactose monolaurate as influenced by various lipases and solvents

Fatty acid sugar esters are non-ionic detergents with multiple uses in the cosmetic, food, and pharmaceutical industries. Of the many different sugar esters synthesized, lactose, a by-product of cheese manufacture, has not been investigated. The objective of this research was to investigate the synthesis of novel lactose monolaurate (LML) and sucrose monolaurate (as a comparison) (SML) using four different immobilized lipases in three different solvents at constant sugar, vinyl laurate, temperature, and enzyme concentrations. Overall, the solvent 2-methyl-2-butanol gave the highest yields and reactions rates for the synthesis of both LML and SML. Of the immobilized lipases, those from Pseudomonas cepacia, Mucor miehei and Thermomyces lanuginosus were effective depending on the sugar/solvent combination. Higher overall yields were obtained for the synthesis of LML with the differences in yields presumably due to the decreased solubility of sucrose as compared to lactose in 3 of the solvents used. Response surface methodology was used to determine the optimal temperature, enzyme concentration and ratio of reactants for LML synthesis using the immobilized lipase from M. miehei in 2-methyl-2-butanol. Based on the analysis of ridge max, the optimal synthesis conditions were predicted to occur at 61 °C, with an enzyme amount of 32 mg/mL, and a molar ratio of lactose to vinyl laurate of 1:3.8; and the optimal actual yield was 99.3%.     

Adding value to a toxic residue from the biodiesel industry: production of two distinct pool of lipases from <Emphasis Type="Italic">Penicillium simplicissimum</Emphasis> in castor bean waste

In countries with a strong agricultural base, such as Brazil, the generation of solid residues is very high. In some cases, these wastes present no utility due to their toxic and allergenic compounds, and so are an environmental concern. The castor bean (Ricinus communis) is a promising candidate for biodiesel production. From the biodiesel production process developed in the Petrobras Research Center using castor bean seeds, a toxic and alkaline waste is produced. The use of agroindustrial wastes in solid-state fermentation (SSF) is a very interesting alternative for obtaining enzymes at low cost. Therefore, in this work, castor bean waste was used, without any treatment, as a culture medium for fungal growth and lipase production. The fungus Penicillium simplicissimum was able to grow and produce an enzyme in this waste. In order to maximize the enzyme production, two sequential designs–Plackett-Burman (variable screening) followed by central composite rotatable design (CCRD)—were carried out, attaining a considerable increase in lipase production, reaching an activity of 155.0 U/g after 96 h of fermentation. The use of experimental design strategy was efficient, leading to an increase of 340% in the lipase production. Zymography showed the presence of different lipases in the crude extract. The partial characterization of such extract showed the occurrence of two lipase pools with distinct characteristics of pH and temperature of action: one group with optimal action at pH 6.5 and 45°C and another one at pH 9.0 and 25°C. These results demonstrate how to add value to a toxic and worthless residue through the production of lipases with distinct characteristics. This pool of enzymes, produced through a low cost methodology, can be applied in different areas of biotechnology.     

Production of structured triacylglycerols by acidolysis catalyzed by lipases immobilized in a packed bed reactor

The aim of this work was to produce structured triacylglycerols (STAGs), with caprylic acid located at positions 1 and 3 of the glycerol backbone and docosohexaenoic acid (DHA) at position 2, by acidolysis of tuna oil and caprylic acid (CA) catalyzed by lipases Rd, from Rhizopus delemar, and Palatase 20000L from Mucor miehei immobilized on Accurel MP1000 in a packed bed reactor (PBR), working in continuous and recirculation modes. First, different lipase/support ratios were tested for the immobilization of lipases and the best results were obtained with ratios of 0.67 (w/w) for lipase Rd and 6.67 (w/w) for Palatase. Both lipases were stable for at least 4 days in the operational conditions. In the storage conditions (5 °C) lipases Rd and Palatase maintained constant activity for 5 months and 1 month, respectively.These catalysts have been used to obtain STAGs by acidolysis of tuna oil and CA in a PBR operating with recirculation of the reaction mixture through the lipase bed. Thus, STAGs with 52–53% CA and 14–15% DHA were obtained. These results were the basis for establishing the operational conditions to obtain STAGs operating in continuous mode. These new conditions were established maintaining constant intensity of treatment (IOT, lipase amount × reaction time/oil amount). In this way STAGs with 44–50% CA and 17–24% DHA were obtained operating in continuous mode. Although the compositions of STAGs obtained with both lipases were similar, Palatase required an IOT about four times higher than lipase Rd.To separate the acidolysis products (free fatty acids, FFAs, and STAGs) an extraction method of FFAs by water–ethanol solutions was tested. The following variables were optimized: water/ethanol ratio (the best results were attained with a water/ethanol ratio of 30:70, w/w), the solvent/FFA–STAG mixture ratio (3:1, w/w) and the number of extraction steps (3–5). In these conditions highly pure STAGs (93–96%) were obtained with a yield of 85%. The residual FFAs can be eliminated by neutralization with a hydroethanolic KOH solution to obtain pure STAGs. The positional analysis of these STAGs, carried out by alcoholysis catalyzed by lipase Novozym 435, has shown that CA represents 55% of fatty acids located at positions 1 and 3 and DHA represents 42% of fatty acids at position 2.     

Physical and stability characteristics of Burkholderia cepacia lipase encapsulated in κ-carrageenan

In this work, a novel approach for lipase immobilization was exploited. Lipase from Burkholderia cepacia was encapsulated into κ-carrageenan by co-extrusion method to form a liquid core capsule. The diameter of the encapsulated lipase was found to be in the range of 1.3–1.8 mm with an average membrane thickness of 200 μm and 5% coefficient of variance. The encapsulation efficiency was 42.6% and 97% moisture content respectively. The encapsulated lipase was stable between pH 6 and 9 and temperature until 50 °C. The encapsulated lipase was stable until disintegration of the carrier when stored at 27 °C and retained 72.3% of its original activity after 6 cycles of hydrolysis of p-NPP. The encapsulated lipase was stable in various organic solvents including methanol, ethanol, iso-propanol, n-hexane and n-heptane. Kinetic parameters K_m and V_max were found to be 0.22 mM and 0.06 μmol/min for free lipase and 0.25 mM and 0.05 μmol/min for encapsulated lipase respectively.     

脂肪酶协同催化猪油合成生物柴油工艺研究

探讨了以乙酸甲酯为酰基受体两种脂肪酶协同催化猪油转酯合成生物柴油的工艺条件。首先利用单因子试验确定2种固定化脂肪酶Novozym435、Lipozyme TLIM单独作为催化剂时的最佳酶用量为40％,反应温度为50℃,乙酸甲酯用量为14（相对于油的摩尔比）。在此基础上,采用3因素5水平和3个中心点的中心组分旋转设计法研究了上述2种脂肪酶协同使用时脂肪酶用量（g/g）、混合酶的配比（%/%）以及乙酸甲酯用量诸因素共同作用对转酯反应转化率的影响。优化后的反应条件为：总酶用量为40％,混合酶配比为50/50,乙酸甲酯用量为14,在该条件下甲酯得率可达97.6％,比同质量的Novozym435、Lipozyme TLIM的催化活性分别高出7.6％、22.3％。表明脂肪酶协同催化猪油合成生物柴油工艺可以较好地提高甲酯得率,并且节约生产成本。     

Application of a Burkholderia cepacia lipase-immobilized silica monolith to batch and continuous biodiesel production with a stoichiometric mixture of methanol and crude Jatropha oil

Background

The enzymatic production of biodiesel through alcoholysis of triglycerides has become more attractive because it shows potential in overcoming the drawbacks of chemical processes. In this study, we investigate the production of biodiesel from crude, non-edible Jatropha oil and methanol to characterize Burkholderia cepacia lipase immobilized in an n-butyl-substituted hydrophobic silica monolith. We also evaluate the performance of a lipase-immobilized silica monolith bioreactor in the continuous production of biodiesel.

Results

The Jatropha oil used contained 18% free fatty acids, which is problematic in a base-catalyzed process. In the lipase-catalyzed reaction, the presence of free fatty acids made the reaction mixture homogeneous and allowed bioconversion to proceed to 90% biodiesel yield after a 12 hour reaction time. The optimal molar ratio of methanol to oil was 3.3 to 3.5 parts methanol to one part oil, with water content of 0.6% (w/w). Further experiments revealed that B. cepacia lipase immobilized in hydrophobic silicates was sufficiently tolerant to methanol, and glycerol adsorbed on the support disturbed the reaction to some extent in the present reaction system. The continuous production of biodiesel was performed at steady state using a lipase-immobilized silica monolith bioreactor loaded with 1.67 g of lipase. The yield of 95% was reached at a flow rate of 0.6 mL/h, although the performance of the continuous bioreactor was somewhat below that predicted from the batch reactor. The bioreactor was operated successfully for almost 50 days with 80% retention of the initial yield.

Conclusions

The presence of free fatty acids originally contained in Jatropha oil improved the reaction efficiency of the biodiesel production. A combination of B. cepacia lipase and its immobilization support, n-butyl-substituted silica monolith, was effective in the production of biodiesel. This procedure is easily applicable to the design of a continuous flow-through bioreactor system.     

Development of an amphiphilic matrix for immobilization of <Emphasis Type="Italic">Candida antartica</Emphasis> lipase B for biodiesel production

Biodiesel has been greatly interested as an alternative fuel and is produced by a transesterification reaction of oil with alcohol. Recently, microbial lipases have been used for biodiesel production. Among the microbial lipase, immobilized Candida antartica lipase B (CALB) is the most widely used. However, CALB is unstable and shows low catalytic efficiency in the reaction media because the reaction media contains a high concentration of methanol and the lipase is also inhibited by the by-product glycerol. In this study, to overcome these limitations, we developed an amphiphilic matrix to immobilize CALB. The immobilized lipase in an amphiphilic matrix with 80% ethyltrimethoxysilane (ETMS) in tetramethoxysilane (TMOS) and pretreated with oil showed the highest specific activity and biodiesel conversion ratio; about 90% biodiesel conversion in 24 h at an initial molar ratio of 1: 1 (oil: methanol) with stepwise methanol feeding in order to adjust the net molar ratio to be 1: 3.     

Proteolytic Activity in Commercial Triacylglycerol Hydrolase Preparations

The proteolytic activity of 34 commercial lipase preparations (CLP) was determined using a labeled casein substrate. Only three CLP were free from proteolytic activity. Porcine pancreatic lipases exhibited levels of proteolytic activity comparable to or greater than that of a reference porcine trypsin. Bacterial lipases contained up to 10% of the proteolytic activity of commercial trypsin. Proteolytic activities in lipases from fungal species were present at low levels (<1% of the activity in trypsin). Among preparations of fungal origin, lipases from Aspergillus niger and Mucor javanicus were highest in proteolytic activity; Aspergillus oryzae and Pseudomonas cepacia lipases were lowest. Proteins in CLP were separated by non-denaturing PAGE; between 4 and 17 protein bands in the range &#104 6.5- &#83 200 kDa were observed. With the exception of a single pair of Rhizomucor miehei lipases, the distribution of apparent molecular weights (AMW) was unique to each preparation. Bands of caseinolytic activity in commercial lipases were visualized by applying a zymographic technique. CLP contained between 0 (P. cepacia lipases) and 6 (porcine pancreas lipase and Rhizopus oryzae lipase) discrete proteolytic bands. Common themes of proteolytic AMW emerged, including 21-23 kDa and 30-35 kDa bands.     

Dynamic modeling of biodiesel production from simulated waste cooking oil using immobilized lipase

The effectiveness of lipase immobilized on ceramic beads, in the production of biodiesel from simulated waste cooking oil in organic solvent system, was compared to that of free lipase. Experimental determination of the effect of concentrations of methanol on the rate of the enzymatic transesterification was experimentally determined. In addition, the effectiveness of lipases from bacterial and yeast sources for biodiesel production from simulated waste cooking oil was compared. A kinetic model was developed to describe the system, taking into consideration the mass transfer resistances of the reactants. Inhibition effects by both substrates on the interfacial reaction were also considered. The experimental results were used to determine the kinetic parameters of the proposed model and to determine the effect of mass transfer. On the other hand, it was shown that biodieasel can be produced in considerable amounts, with yield reaching 40%, in absence of organic solvent using immobilized lipase from P. cepacia on ceramic beads.     

Sustainable preparation of a novel glycerol-free biofuel by using pig pancreatic lipase: Partial 1,3-regiospecific alcoholysis of sunflower oil

The preparation of a novel biofuel denoted as Ecodiesel-100 from the partial 1,3-regiospecific alcoholysis of sunflower oil is reported. Pig pancreatic lipase (PPL) was employed in the reaction as both free and immobilised enzyme on sepiolite. The resulting biofuel is composed of fatty acid ethyl esters and monoglycerides (FAEE/MG) blended in a molar relation 2/1. The novel biofuel has similar physico-chemical properties compared to those of conventional biodiesel and/or petrodiesel, avoiding the production of glycerine as by-product.The biocatalyst was found to be strongly fixed to the inorganic support (87.5%). Nevertheless, the efficiency of the immobilised enzyme was reduced to less than half (42%) compared to that of the free PPL. Quantitative conversions of triglycerides and high yields to FAEE were obtained under mild reaction conditions (20–80 °C, oil/alcohol 2/1 v:v ratio and PPL 0.01–0.1% w/w of total substrate). The immobilised enzyme showed a remarkable stability as well as a great reusability (more than 11 successive reuses) without a significant loss of its initial catalytic activity. Both immobilised and free enzyme exhibited the same reaction mechanism, according to the coincidental results in the Arrhenius parameters (Ln A and E_a). The immobilised PPL was found to be very suitable for the continuous production of biofuel due to its facile recyclability from the reaction mixture.     

Amino acid modified chitosan beads: Improved polymer supports for immobilization of lipase from Candida rugosa

Amino acid modified chitosan beads (CBs) for immobilization of lipases from Candida rugosa were prepared by activation of a chitosan backbone with epichlorohydrin followed by amino acid coupling. The beads were analyzed by elemental analysis and solid state NMR with coupling yields of the amino acids ranging from 15 to 60%. The immobilized lipase on unmodified chitosan beads showed the highest immobilization yield (92.7%), but its activity was relatively low (10.4%). However, in spite of low immobilization yields (15–50%), the immobilized lipases on the amino acid modified chitosan beads showed activities higher than that of the unmodified chitosan beads, especially on Ala or Leu modified chitosan beads (Ala-CB or Leu-CB) with 49% activity for Ala-CB and 51% for Leu-CB. The immobilized lipases on Ala-CB improved thermal stability at 55 °C, compared to free and immobilized lipases on unmodified chitosan beads and the immobilized lipase on Ala-CB retained 93% of the initial activity when stored at 4 °C for 4 weeks. In addition, the activity of the immobilized lipase on Ala-CB retained 77% of its high initial activity after 10 times of reuse. The kinetic data (k_cat/K_m) supports that the immobilized lipase on Ala-CB can give better substrate specificity than the unmodified chitosan beads.     

Poly(ethylene glycol)-lipase complex that is catalytically active for alcoholysis reactions in ionic liquids

Lipase-catalyzed alcoholysis was investigated in three different ionic liquids. Lyophilized native lipase had a low activity in all the ionic liquids but a poly(ethylene glycol) (PEG)-lipase complex (with a molar ratio of the polymer/enzyme of 10:1) had an increased activity of over 14-fold. Of several lipases tested, PEG-lipase PS (from Pseudomonas cepacia) exhibited the highest activity (1.07 mmol/(h g^–1 protein)) in 1-octyl-3-methylimidazolium hexafluorophosphate.     

Synthesis and characterization of cyclodextrin-based polymers as a support for immobilization of Candida rugosa lipase

The objective of this study was to prepare cross-linked β-cyclodextrin polymers for immobilization of Candida rugosa lipase. The structures of synthesized macrocyclic compounds were characterized by Fourier transform infrared spectroscopy (FTIR), thermal gravimetric analysis (TGA) and scanning electron microscope (SEM) techniques. Properties of the immobilized systems were assessed and their performance on hydrolytic reaction were evaluated and compared with the free enzyme. The influence of activation agents (glutaraldehyde (GA) and hexamethylene diisocyanate (HMDI)) and thermal and pH stabilities of the biocatalyst was evaluated. After the optimization of immobilization process, the physical and chemical characterization of immobilized lipase was performed. Obtained data showed that the immobilized enzyme seemed better and offered some advantages in comparison with free enzyme. It can be observed that the free lipase loses its initial activity within around 80 min at 60 °C, while the immobilized lipases retain their initial activities of about 56% by HMDI and 82% by GA after 120 min of heat treatment at 60 °C.Results showed that the specific activity of the immobilized lipase with glutaraldehyde was 62.75 U/mg protein, which is 28.13 times higher than that of the immobilized lipase with HMDI.     

Enzymatic coproduction of biodiesel and glycerol carbonate from soybean oil and dimethyl carbonate

The enzymatic coproduction of biodiesel and glycerol carbonate by the transesterification of soybean oil was studied using lipase as catalyst in organic solvent. To produce biodiesel and glycerol carbonate simultaneously, experiments were designed sequentially. Enzyme screening, the molar ratio of dimethyl carbonate (DMC) to soybean oil, reaction temperature and solvent effects were investigated. The results of enzyme screening, at 100 g/L Novozym 435 (immobilized Candida antarctica lipase B), biodiesel and glycerol carbonate showed conversions of 58.7% and 50.7%, respectively. The optimal conditions were 60 °C, 100 g/L Novozym 435, 6.0:1 molar ratio with tert-butanol as solvent: 84.9% biodiesel and 92.0% glycerol carbonate production was achieved.