Esterification using a liquid lipase to remove residual free fatty acids in biodiesel

Lately, the price of liquid formulated lipase enzymes, usable in biodiesel production, has been significantly reduced. This enables one-time use of these enzymes for transesterification, and the process is used industrially. However, the process suffers a drawback by leaving 2−3 % free fatty acids in the crude biodiesel, which reduces the profitability. This article discusses a novel enzymatic FFA esterification reaction utilizing liquid lipase B from Candida antarctica (CALB) along with glycerol at low water concentrations to eliminate the residual FFA. The reaction setup was found able to reduce the free fatty acid concentration to within biodiesel specifications of < 0.25 wt.% FFA. Additionally, two alternative process setups are proposed, which were both found viable through a combination of experiments and simulations, and can be developed into full-scale processes. The resulting two-step enzymatic biodiesel process - transesterification followed by esterification - provides a potential process layout for the industrial production of biodiesel.     

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.     

Production of algae-based biodiesel using the continuous catalytic Mcgyan® process

This study demonstrates the production of algal biodiesel from Dunaliella tertiolecta, Nannochloropsis oculata, wild freshwater microalgae, and macroalgae lipids using a highly efficient continuous catalytic process. The heterogeneous catalytic process uses supercritical methanol and porous titania microspheres in a fixed bed reactor to catalyze the simultaneous transesterification and esterification of triacylglycerides and free fatty acids, respectively, to fatty acid methyl esters (biodiesel). Triacylglycerides and free fatty acids were converted to alkyl esters with up to 85% efficiency as measured by 300 MHz ¹H NMR spectroscopy. The lipid composition of the different algae was studied gravimetrically and by gas chromatography. The analysis showed that even though total lipids comprised upwards of 19% of algal dry weight the saponifiable lipids, and resulting biodiesel, comprised only 1% of dry weight. Thus highlighting the need to determine the triacylglyceride and free fatty acid content when considering microalgae for biodiesel production.     

Statistical analysis and optimization of biodiesel production from waste coffee grounds by a two-step process

Biodiesel was produced using waste coffee grounds (WCGs) via a two-step process comprising lipid extraction and subsequent transesterification steps. Each step was statistically analyzed, and optimum conditions for each step were suggested. WCGs were found to have 16.4% lipid content with 1.9% free fatty acid (FFA) content. The liquid-solid ratio (LSR) significantly influenced lipid extraction from WCGs, while extraction time and temperature did not; 92.7% of lipid extraction efficiency was achieved at 13.7 mL-hexane/g-WCGs, 30 min of extraction time, and 25°C. Owing to the relatively low FFA content, an alkaline catalyst (NaOH) reaction was used that requires less amount of catalyst, methanol, and shorter reaction time compared to an acid catalyst reaction. Reaction time and temperature were the major factors affecting biodiesel conversion, and 94.0% of biodiesel conversion was obtained at optimum conditions for transesterification: 0.5% catalyst, 1.5 mL-methanol/g-lipid, 45°C, and 9 h of reaction time. With the use of statistical analysis tools, high lipid extraction efficiency and biodiesel conversion were achieved at relatively mild conditions, which would reduce biodiesel production cost substantially.     

Two-step synthesis of fatty acid ethyl ester from soybean oil catalyzed by <Emphasis Type="Italic">Yarrowia lipolytica</Emphasis> lipase

Background  

Enzymatic biodiesel production by transesterification in solvent media has been investigated intensively, but glycerol, as a by-product, could block the immobilized enzyme and excess n-hexane, as a solution aid, would reduce the productivity of the enzyme. Esterification, a solvent-free and no-glycerol-release system for biodiesel production, has been developed, and two-step catalysis of soybean oil, hydrolysis followed by esterification, with Yarrowia lipolytica lipase is reported in this paper.     

Conversion of acid oil by-produced in vegetable oil refining to biodiesel fuel by immobilized Candida antarctica lipase

Acid oil, which is a by-product in vegetable oil refining, mainly contains free fatty acids (FFAs) and acylglycerols, and is a candidate of materials for production of biodiesel fuel. A mixture (acid oil model) of refined FFAs and vegetable oil was recently reported to be converted to fatty acid methyl esters (FAMEs) at >98% conversion by a two-step reaction system comprising methyl esterification of FFAs and methanolysis of acylglycerols using immobilized Candida antarctica lipase. The two-step system was thus applied to conversion of acid oil by-produced in vegetable oil refining to biodiesel fuel. Under similar conditions that were determined by using acid oil model, however, the lipase was unstable and was not durable for repeated use. The inactivation of the lipase was successfully avoided by addition of excess amounts of methanol (MeOH) in the first-step reaction, and by addition of vegetable oil and glycerol in the second-step reaction. Hence, the first-step reaction was conducted by shaking a mixture of 66 wt% acid oil (77.9 wt% FFAs, 10.8 wt% acylglycerols) and 34 wt% MeOH with 1 wt% immobilized lipase, to convert FFAs to their methyl esters. The second-step reaction was performed by shaking a mixture of 52.3 wt% dehydrated first-step product (79.7 wt% FAMEs, 9.7 wt% acylglycerols), 42.2 wt% rapeseed oil, and 5.5 wt% MeOH using 6 wt% immobilized lipase in the presence of additional 10 wt% glycerol, to convert acylglycerols to FAMEs. The resulting product was composed of 91.1 wt% FAMEs, 0.6 wt% FFAs, 0.8 wt% triacylglycerols, 2.3 wt% diacylglycerols, and 5.2 wt% other compounds. Even though each step of reaction was repeated every 24 h by transferring the immobilized lipase to the fresh substrate mixture, the composition was maintained for >100 cycles.     

An integrated approach to produce biodiesel and monoglycerides by enzymatic interestification of babassu oil (Orbinya sp)

Two screenings of commercial lipases were performed to find a lipase with superior performance for the integrated production of biodiesel and monoglycerides. The first screening was carried out under alcoholysis conditions using ethanol as acyl acceptor to convert triglycerides to their corresponding ethyl esters (biodiesel). The second screening was performed under glycerolysis conditions to yield monoglycerides (MG). All lipases were immobilized on silica–PVA composite by covalent immobilization. The assays were performed using babassu oil and alcohols (ethanol or glycerol) in solvent free systems. For both substrates, lipase from Burkholderia cepacia (lipase PS) was found to be the most suitable enzyme to attain satisfactory yields. To further improve the process, the Response Surface Methodology (RSM) was used to determine the optima operating conditions for each biotransformation. For biodiesel production, the highest transesterification yield (>98%) was achieved within 48 h reaction at 39 °C using an oil-to-ethanol molar ratio of 1:7. For MG production, optima conditions corresponded to oil-to-glycerol molar ratio of 1:15 at 55 °C, yielding 25 wt.% MG in 6 h reaction. These results show the potential of B. cepacia lipase to catalyze both reactions and the feasibility to consider an integrated approach for biodiesel and MG production.     

Simultaneous conversion of free fatty acids and triglycerides to biodiesel by immobilized Aspergillus oryzae expressing Fusarium heterosporum lipase

The presence of high levels of free fatty acids (FFA) in oil is a barrier to one‐step biodiesel production. Undesirable soaps are formed during conventional chemical methods, and enzyme deactivation occurs when enzymatic methods are used. This work investigates an efficient technique to simultaneously convert a mixture of free fatty acids and triglycerides (TAG). A partial soybean hydrolysate containing 73.04% free fatty acids and 24.81% triglycerides was used as a substrate for the enzymatic production of fatty acid methyl ester (FAME). Whole‐cell Candida antarctica lipase B‐expressing Aspergillus oryzae, and Novozym 435 produced only 75.2 and 73.5% FAME, respectively. Fusarium heterosporum lipase‐expressing A. oryzae produced more than 93% FAME in 72 h using three molar equivalents of methanol. FFA and TAG were converted simultaneously in the presence of increasing water content that resulted from esterification. Therefore, F. heterosporum lipase with a noted high level of tolerance of water could be useful in the industrial production of biodiesel from feedstock that has high proportion of free fatty acids.     

Acyl migration and kinetics study of 1(3)-positional specific lipase of Rhizopus oryzae-catalyzed methanolysis of triglyceride for biodiesel production

The lipase of Rhizopus oryzae (R. oryzae) was reported to have 1(3)-positional specificity, but in the process of R. oryzae-catalyzed biodiesel production, the yield of biodiesel (methyl esters) could reach over 80%. Although during 1(3)-positional specific lipase-catalyzed methanolysis of triglycerides, acyl migration was thought as one of the major reasons for higher methyl ester yield, there was no further study on the mechanism exploration regarding to acyl migration. In this paper, acyl migration and the related kinetics of R. oryzae-mediated methanolysis of triolein was studied systematically. Through our study, it was revealed that during the methanolysis process, acyl migration between 2-MG and 1-MG as well as acyl migration between 1,2-DG and 1,3-DG could take place independent of enzymatic catalysis. The kinetic study showed that the acyl migration was first-order reversible reaction. Based on this finding, a two-step mechanic model including acyl migration was developed for the enzyme-mediated methanolysis for biodiesel production and it was found that the reaction included consecutive hydrolysis and esterification. Further investigation on kinetics showed that R. oryzae lipase was not restrict selectivity of 1(3)-position acyl group, but a preference of 1(3)-position over 2-position, which also contributed to the higher yield of methyl esters.     

Lipid Profile Remodeling in Response to Nitrogen Deprivation in the Microalgae Chlorella sp. (Trebouxiophyceae) and Nannochloropsis sp. (Eustigmatophyceae)

Many species of microalgae produce greatly enhanced amounts of triacylglycerides (TAGs), the key product for biodiesel production, in response to specific environmental stresses. Improvement of TAG production by microalgae through optimization of growth regimes is of great interest. This relies on understanding microalgal lipid metabolism in relation to stress response in particular the deprivation of nutrients that can induce enhanced TAG synthesis. In this study, a detailed investigation of changes in lipid composition in Chlorella sp. and Nannochloropsis sp. in response to nitrogen deprivation (N-deprivation) was performed to provide novel mechanistic insights into the lipidome during stress. As expected, an increase in TAGs and an overall decrease in polar lipids were observed. However, while most membrane lipid classes (phosphoglycerolipids and glycolipids) were found to decrease, the non-nitrogen containing phosphatidylglycerol levels increased considerably in both algae from initially low levels. Of particular significance, it was observed that the acyl composition of TAGs in Nannochloropsis sp. remain relatively constant, whereas Chlorella sp. showed greater variability following N-deprivation. In both algae the overall fatty acid profiles of the polar lipid classes were largely unaffected by N-deprivation, suggesting a specific FA profile for each compartment is maintained to enable continued function despite considerable reductions in the amount of these lipids. The changes observed in the overall fatty acid profile were due primarily to the decrease in proportion of polar lipids to TAGs. This study provides the most detailed lipidomic information on two different microalgae with utility in biodiesel production and nutraceutical industries and proposes the mechanisms for this rearrangement. This research also highlights the usefulness of the latest MS-based approaches for microalgae lipid research.     

Evaluation of immobilized lipases on poly-hydroxybutyrate beads to catalyze biodiesel synthesis

Five microbial lipase preparations from several sources were immobilized by hydrophobic adsorption on small or large poly-hydroxybutyrate (PHB) beads and the effect of the support particle size on the biocatalyst activity was assessed in the hydrolysis of olive oil, esterification of butyric acid with butanol and transesterification of babassu oil (Orbignya sp.) with ethanol. The catalytic activity of the immobilized lipases in both olive oil hydrolysis and biodiesel synthesis was influenced by the particle size of PHB and lipase source. In the esterification reaction such influence was not observed. Geobacillus thermocatenulatus lipase (BTL2) was considered to be inadequate to catalyze biodiesel synthesis, but displayed high esterification activity. Butyl butyrate synthesis catalyzed by BTL2 immobilized on small PHB beads gave the highest yield (≈90 mmol L(-1)). In biodiesel synthesis, the catalytic activity of the immobilized lipases was significantly increased in comparison to the free lipases. Full conversion of babassu oil into ethyl esters was achieved at 72 h in the presence of Pseudozyma antarctica type B (CALB), Thermomyces lanuginosus lipase (Lipex(?) 100 L) immobilized on either small or large PHB beads and Pseudomonas fluorescens (PFL) immobilized on large PHB beads. The latter preparation presented the highest productivity (40.9 mg of ethyl esters mg(-1) immobilized protein h(-1)).     

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%).     

Lipase-catalysed synthesis of ester oils from biodiesel by-products

Ester oils obtained from natural long-chain fatty acids and alcohols are versatile substitutes for many petroleum-based products. Their efficient synthesis with the solvent-free esterification of free fatty acids (FFA) from by-products of biodiesel fabrication and 2-ethyl-1-hexanol with immobilised lipase from Thermomyces lanuginosa was investigated. The immobilisation of the biocatalyst in static emulsion yielded a specific esterification activity that was higher by a factor of 4.9–9.4 than the activity of the native enzyme. Favourable properties of the silicone-based immobilisation matrix in terms of stability and immobilisation yield were observed. In biodiesel by-products, the immobilised lipase catalysed the esterification of FFA as well as the transesterification of residual fatty acid methyl esters (FAME) to the desired ester oils. A conversion of 90% FFA and 35% FAME gave a total yield of 60%. The inactivation coefficients during repeated use in a stirred-tank reactor with intermittent pressure reduction were exceptionally low.     

Enzymatic fractionation of conjugated linoleic acid isomers by selective esterification

Attempt was done to prepare food supplements with high content of c9, t11-CLA or t10, c12-CLA. A free acid mixture containing CLA isomers was esterified with ethanol by enzyme catalysis. Novozyme 435 and Lipase AY30 were screened, and Lipase AY30 was employed to catalyze esterification reaction because of its high fractionation efficiency. Effect of reaction conditions on total esterification was investigated, and the optimal reaction conditions were: 140 U of lipase amount, reaction temperature at 50 °C, a pH of 6.5, and molar ratio of FFA–CLA to ethanol at 1:1. Based on the studies above, experiments of esterification and purification were done, and the best fractionation efficiency was obtained when the total esterification was 37%, and the corresponding purity and recovery of c9, t11-CLA were 75.50 and 49.85%, and that of t10, c12-CLA were 72.02 and 62.32%.     

Two-step biodiesel production from Calophyllum inophyllum oil: Optimization of modified β-zeolite catalyzed pre-treatment

In this study, a two-step process was developed to produce biodiesel from Calophyllum inophyllum oil. Pre-treatment with phosphoric acid modified β-zeolite in acid catalyzed esterification process preceded by transesterification which was done using conventional alkali catalyst potassium hydroxide (KOH). The objective of this study is to investigate the relationship between the reaction temperatures, reaction time and methanol to oil molar ratio in the pre-treatment step. Central Composite Design (CCD) and Response Surface Methodology (RSM) were utilized to determine the best operating condition for the pre-treatment step. Biodiesel produced by this process was tested for its fuel properties.     

Efficient solvothermal wet in situ transesterification of Nannochloropsis gaditana for biodiesel production

In situ transesterification of wet microalgae is a promising, simplified alternative biodiesel production process that replaces multiple operations of cell drying, extraction, and transesterification reaction. This study addresses enhanced biodiesel production from Nannochloropsis gaditana at elevated temperatures. Compared with the previously reported in situ transesterification process of conducting the reaction at a temperature ranging from 95 to 125 °C, the present work employs higher temperatures of at least 150 °C. This relatively harsh condition allows much less acid catalyst with or without co-solvent to be used during this single extraction-conversion process. Without any co-solvent, 0.58% (v/v) of H₂SO₄ in the reaction medium can achieve 90 wt% of the total lipid conversion to biodiesel at 170 °C when the moisture content of wet algal paste is 80 wt%. Here, the effects of temperature, acid catalyst, and co-solvent on the FAEE yield and specification were scrutinized, and the reaction kinetic was investigated to understand the solvothermal in situ transesterification reaction at the high temperature. Having a biphasic system (water/chloroform) during the reaction also helped to meet biodiesel quality standard EN 14214, as Na⁺, K⁺, Ca²⁺, Mg²⁺ cations and phosphorus were detected only below 5 ppm. With highlights on the economic feasibility, wet in situ transesterification at the high temperature can contribute to sustainable production of biodiesel from microalgae by reducing the chemical input and relieve the burden of extensive post purification process, therefore a step towards green process.

     

Immobilization of steapsin lipase on macroporous immobead-350 for biodiesel production in solvent free system

Commercially available steapsin lipase was immobilized on macroporous polymer beads (IB-350) and further investigated for biodiesel production under solvent free conditions. The fatty acid methyl ester (biodiesel) synthesis was carried out by the methanolysis of fresh and used cooking sunflower oil. The enzymatic reaction for biodiesel synthesis was optimized with various reaction parameters and the obtained reaction conditions were 1: 6 molar ratio (oil: methanol), 50 mg biocatalyst and 20% water content at 45°C for 48 h under solvent free conditions. It was observed that 94% of biodiesel was produced under the optimized reaction conditions. The four step addition of methanol at the interval of 12 h was found to be more effective. Moreover the biocatalyst was effectively reused for four consecutive recycles and was appreciably stable for 90 days. The results obtained highlight potential of immobilized steapsin lipase for biodiesel production.     

Expression of a lipid-inducible,self-regulating form of <Emphasis Type="Italic">Yarrowia lipolytica</Emphasis> lipase <Emphasis Type="Italic">LIP2</Emphasis> in <Emphasis Type="Italic">Saccharomyces cerevisiae</Emphasis>

Saccharomyces cerevisiae is frequently used as a bioreactor for conversion of exogenously acquired metabolites into value-added products, but has not been utilized for bioconversion of low-cost lipids such as triacylglycerols (TAGs) because the cells are typically unable to acquire these lipid substrates from the growth media. To help circumvent this limitation, the Yarrowia lipolytica lipase 2 (LIP2) gene was cloned into S. cerevisiae expression vectors and used to generate S. cerevisiae strains that secrete active Lip2 lipase (Lip2p) enzyme into the growth media. Specifically, LIP2 expression was driven by the S. cerevisiae PEX11 promoter, which maintains basal transgene expression levels in the presence of sugars in the culture medium but is rapidly upregulated by fatty acids. Northern blotting, lipase enzyme activity assays, and gas chromatographic measurements of cellular fatty acid composition after lipid feeding all confirmed that cells transformed with the PEX11 promoter–LIP2 construct were responsive to lipids in the media, i.e., cells expressing LIP2 responded rapidly to either free fatty acids or TAGs and accumulated high levels of the corresponding fatty acids in intracellular lipids. These data provided evidence of the creation of a self-regulating positive control feedback loop that allows the cells to upregulate Lip2p production only when lipids are present in the media. Regulated, autonomous production of extracellular lipase activity is a necessary step towards the generation of yeast strains that can serve as biocatalysts for conversion of low-value lipids to value-added TAGs and other novel lipid products.     

One-step enzymatic production of fatty acid ethyl ester from high-acidity waste feedstocks in solvent-free media

This work aims to demonstrate the enzymatic production of fatty acid ethyl ester biodiesel from highly acidic feedstock in a single-step reaction, without co-solvents and avoiding the inhibition of the enzyme by ethanol and glycerol. Additionally, an empirical equation is proposed to predict the kinetics of the production reaction as a function of the used feedstock and catalyst concentration. Biodiesel production from highly acidic feedstock perform via simultaneous esterification of free fatty acids and transesterification of triacylglycerols. Enzymatic catalysis is one of the most promising alternative technologies for the biodiesel production. Increasing of the enzymatic bioactivity is crucial for the success of such process in industrial scale. Currently, stepwise addition of the alcohol or the use of co-solvents have been proposed to avoid enzyme inhibition, such strategies add downstream processes to the production. These results can be applied to the development economical-viable enzymatic production of biodiesel in industrial scale.