Biodiesel production by two-stage transesterification with ethanol

A two-stage process consisting of two reactions steps with glycerin separation and ethanol/catalyst addition in each of them was optimized for ethyl esters production. The optimal reaction temperature was 55 °C. At an ethanol/oil molar ratio of 4.25:1 (25%v/v alcohol with respect to oil), a 99% conversion value was obtained with low ethanol consumption. In contrast to methoxide catalysts, sodium and potassium hydroxide catalysts severely complicate the purification since no phase separation took place under most conditions. With a total sodium methoxide concentration of 1.06 g catalyst/100 g oil, and adding 50% of the catalyst in each reaction step, biodiesel with a total glycerin content of 0.172% was obtained. The optimal conditions found in this study make it possible to use the same industrial facility to produce either methyl or ethyl esters.     

Biodiesel production by transesterification using immobilized lipase

Biodiesel can be produced by transesterification of vegetable or waste oil catalysed by lipases. Biodiesel is an alternative energy source to conventional fuel. It combines environmental friendliness with biodegradability, low toxicity and renewability. Biodiesel transesterification reactions can be broadly classified into two categories: chemical and enzymatic. The production of biodiesel using the enzymatic route eliminates the reactions catalysed under acid or alkali conditions by yielding product of very high purity. The modification of lipases can improve their stability, activity and tolerance to alcohol. The cost of lipases and the relatively slower reaction rate remain the major obstacles for enzymatic production of biodiesel. However, this problem can be solved by immobilizing the enzyme on a suitable matrix or support, which increases the chances of re-usability. The main factors affecting biodiesel production are composition of fatty acids, catalyst, solvents, molar ratio of alcohol and oil, temperature, water content, type of alcohol and reactor configuration. Optimization of these parameters is necessary to reduce the cost of biodiesel production.     

Integrated production for biodiesel and 1,3-propanediol with lipase-catalyzed transesterification and fermentation

Biodiesel, a renewable alternative to fossil energy, has shown great prospects for global proliferation in the past decade. Lipase catalyzed transesterification for biodiesel production, as a biological process with many advantages has drawn increasing attention. As a by-product, glycerol accounts for about 10% w/w of biodiesel during the process of biodiesel production. As a result, the conversion of glycerol has become a common problem which has to be resolved if considering large amount of biodiesel production. Glycerol can be fermented into 1,3-propanediol, a high value added chemical with a promising future in the polymers, for example, polytrimethylene terephthalate, and also fermentation approaches for 1,3-propanediol production which have drawn more and more attention due to advantages such as relatively low investment, mild reaction conditions and using renewable sources as the starting materials. Based on the latest technology advancements in lipase-mediated transformation for biodiesel production, the aerobic fermentation technology and genetic engineering for 1,3-propanediol production, and the integrated production of 1,3-propanediol from crude glycerol could be a promising way to improve the profit of the whole process during biodiesel production.     

Biodiesel production through lipase catalyzed transesterification: An overview

Recently, with the global shortage of fossil fuels, excessive increase in the price of crude oil and increased environmental concerns have resulted in the rapid growth in biodiesel production. The central reaction in the biodiesel production is the transesterification reaction which could be catalyzed either chemically or enzymatically. Enzymatic transesterification has certain advantages over the chemical catalysis of transesterification, as it is less energy intensive, allows easy recovery of glycerol and the transesterification of glycerides with high free fatty acid contents. Limitations of the enzyme catalyzed reactions include high cost of enzyme, low yield, high reaction time and the amount of water and organic solvents in the reaction mixture. Researchers have been trying to overcome these limitations in the enzyme catalyzed transesterification reaction. This paper is meant to review the latest development in the field of lipase catalyzed transesterification of biologically derived oil to produce biodiesel.     

Biodiesel fuel production via transesterification of oils using lipase biocatalyst

Biodiesel has gained widespread importance in recent years as an alternative, renewable liquid transportation fuel. It is derived from natural triglycerides in the presence of an alcohol and an alkali catalyst via a transesterification reaction. To date, transesterification based on the use of chemical catalysts has been predominant for biodiesel production at the industrial scale due to its high conversion efficiency at reasonable cost. Recently, biocatalytic transesterification has received considerable attention due to its favorable conversion rate and relatively simple downstream processing demands for the recovery of by-products and purification of biodiesel. Biocatalysis of the transesterification reaction using commercially purified lipase represents a major cost constraint. However, more cost-effective techniques based on the immobilization of both extracellular and intracellular lipases on support materials facilitate the reusability of the catalyst. Other variables, including the presence of alcohol, glycerol and the activity of water can profoundly affect lipase activity and stability during the reaction. This review evaluates the current status for lipase biocatalyst-mediated production of biodiesel, and identifies the key parameters affecting lipase activity and stability. Pioneer studies on reactor-based lipase conversion of triglycerides are presented.     

Terpene ester synthesis by lipase-catalyzed transesterification

Summary Five lipases were screened for their ability to synthesize terpene esters by transesterification. The nature of terpene alcohol and enzyme, as well as the chain length of the acyl donor used affected the product yields. Lipase AY from Candida rugosa gave the best overall yield (96.2%). Geraniol and tributyrin were also found to be the best reactants.     

Biodiesel production by in situ transesterification of municipal primary and secondary sludges

The potential of using municipal wastewater sludges as a lipid feedstock for biodiesel production was investigated. Primary and secondary sludge samples obtained from a municipal wastewater treatment plant in Tuscaloosa, AL were freeze-dried and subjected to an acid-catalyzed insitu transesterification process. Experiments were conducted to determine the effects of temperature, sulfuric acid concentration, and mass ratio of methanol to sludge on the yield of fatty acid methyl esters (FAMEs). Results indicated a significant interactive effect between temperature, acid concentration, and methanol to sludge mass ratio on the FAME yield for the insitu transesterification of primary sludge, while the FAME yield for secondary sludge was significantly affected by the independent effects of the three factors investigated. The maximum FAME yields were obtained at 75 degrees C, 5% (v/v) H(2)SO(4), and 12:1 methanol to sludge mass ratio and were 14.5% and 2.5% for primary and secondary sludge, respectively. Gas chromatography (GC) analysis of the FAMEs revealed a similar fatty acid composition for both primary and secondary sludge. An economic analysis estimated the cost of $3.23/gallon for a neat biodiesel obtained from this process at an assumed yield of 10% FAMEs/dry weight of sludge.     

Design of phosphonium ionic liquids for lipase-catalyzed transesterification

Ionic liquids are now recognized as solvents for use in lipase-catalyzed reactions; however, there still remains a serious drawback in that the rate of reaction in an ionic liquid is slower than that in a conventional organic solvent. To overcome this problem, attempts have been made to evolve phosphonium ionic liquids appropriate for lipase-catalyzed reaction; several types of phosphonium salts have been prepared and their capability evaluated for use as solvent for the lipase-catalyzed reaction. Very rapid lipase PS-catalyzed transesterification of secondary alcohols was obtained when 2-methoxyethyl(tri-n-butyl)phosphonium bis(trifluoromethanesulfonyl)imide ([MEBu₃P][NTf₂]) was used as solvent, affording the first example of a reaction rate superior to that in diisopropyl ether.     

Glucoamylase production in continuous cultures of Aspergillus niger with special emphasis on growth parameters

World Journal of Microbiology and Biotechnology - Maltose-limited continuous culture of Aspergillus niger was carried out with potassium nitrate to investigate growth and glucoamylase formation...     

Glucoamylase production in continuous cultures of Aspergillus niger with special emphasis on growth parameters

Maltose-limited continuous culture of Aspergillus niger was carried out with potassium nitrate to investigate growth and glucoamylase formation characteristics. Glucoamylase production was dependent on the specific growth rate. The maximal amount of glucoamylase (units/l and U/g dry weight) was obtained at =0.08h–1, and the maximum specific rate of production (units/g/dry weight per hour) was at =0.2h–1. The maintenance coefficients (ms and mATP) were higher than for some other fungi. Maximal growth yields on substrate, oxygen and ATP (Yxsm, YxO2m and Yxam) were very efficient (high) and the value of Yxam, which cannot exceed the theoretical maximal value, is obtained when a P/O ratio of 1:1 is assumed. This indicates that biomass formation is energetically inexpensive and most of the expended energy has to be invested in the process of glucoamylase excretion.     

Synthesis of D-allose fatty acid esters via lipase-catalyzed regioselective transesterification

The acylation of the rare sugar, D-allose (the C-3 epimer of D-glucose), with fatty acid vinyl esters was successfully carried out using Candida antarctica lipase in acetonitrile at 45 degrees C to give D-allose 6-alkanoates with high regioselectivity in good yields.     

Effect of reaction parameters on synthesis of citronellyl methacrylate by lipase-catalyzed transesterification

The methacrylate ester of citronellol was synthesized using various lipases as catalyst. The effect of different reaction parameters such as amount of lipase, solvent, temperature, and acylating agent on the conversion of citronellol to citronellyl methacrylate was studied. Methyl methacrylate, vinyl methacrylate, and 2,3-butanedione mono-oxime methacrylate were used as acylating agents. Porcine pancreatic lipase (PPL), Candida rugosa lipase (CRL), and Pseudomonas cepacia lipase (Amano-PS) were used as biocatalysts. Diisopropyl ether (DIPE) was found to be the most suitable solvent. The stereoselectivity of CRL in transesterification of (+/-)-citronellol was tested for the optimized reaction parameters.     

Engineering of lipase-catalyzed transesterification reaction media using water and diethylamine

The objective of presented study was to maximize yields of 2-methylbutyl esters, derived by transesterification reactions mediated by sn-1,3-specific lipases, through engineering of reaction medium. Effects of water and diethylamine (DEA) concentrations on the efficiency of plant oils 2-methylbutanolysis, catalyzed by either mycelium-bound Mucor circinelloides lipase (powder) or commercial immobilized lipase Lipozyme TL IM, were determined. Water content monitoring in reaction mixtures enabled to optimize the initial water content in terms of preventing the dehydration of enzyme’s microenvironment and increasing 2-methylbutyl esters yields. These yields were found to be increased by addition of either suitable amounts of water (0.5–1.5%) or diethylamine (10–30?mM) to the mixture of substrates. The presented results suggest that at low concentrations, diethylamine molecules contribute to retaining water in the microenvironment of enzyme that gives rise to increased transesterification yields and significantly reduced amounts of residual mono- and 1,2-diacyl-glycerols.     

Molecular modeling of the enantioselectivity in lipase-catalyzed transesterification reactions.

Two strategies based on the use of subsets for calculating the enantioselectivity in lipase-catalyzed transesterifications using the CHARMM force field were investigated. Molecular dynamics was used in our search for low energy conformations. Molecular mechanics was used for refining these low energy conformations. A tetrahedral intermediate with a rigid central part was used for mimicking the transition state. The energy differences between the transition states of the diastereomeric enzyme-substrate complexes were calculated. The way of defining the subsets was based on two fundamentally different strategies. The first strategy used predefined parts of the enzyme and the substrate as subsets. The second approach formed energy-based subsets, varying in size with the substrates studied. The selection of residues to be included in these energy-based subsets was based on the energy of the interaction between the specific residue or water molecule and the transition state. The reaction studied was the kinetic resolution of secondary alcohols in transesterifications using the Candida antarctica lipase B as chiral biocatalyst. The secondary alcohols used in the study were 2-butanol, 3-methyl-2-butanol, and 3,3-dimethyl-2-butanol.     

Study of vitamin ester synthesis by lipase-catalyzed transesterification in organic media

Immobilized lipase from Candida antarctica (Novozym 435) was used in organic media to catalyze esterifications of vitamins (ascorbic acid and retinol) from hydroxy acid. We described the synthesis of retinyl L-lactate by transesterification between retinol and L-methyl lactate with yield reaching 90% and the synthesis of ascorbyl L-lactate by transesterification between ascorbic acid and L-methyl lactate with yield reaching 80%. The kinetic study of the esterification of vitamins with L-methyl lactate in organic media has been carried out and agrees with ping-pong-ordered Bi-Bi when the initial vitamin concentration is low. When initial vitamin concentration is high, the kinetic is similar to a hybrid ping-pong-ordered Bi Bi or hybrid ping-pong-random Bi Bi mechanism. However, with high initial substrate concentration, change of the kinetic by other phenomena, such as interaction of substrates with molecular sieves, adsorption of the methanol formed, and decreases of substrate diffusion, could be considered. It is obvious that in these conditions, classical enzymology (i.e., Michaelian enzymology) cannot be used for the interpretation of results.     

Synthesis of the immunosuppressive agent 2-morpholinoethyl mycophenolate by a lipase-catalyzed transesterification

The synthesis of 2-morpholinoethyl mycophenolate was realized by an enzymatic transesterification of simple esters of mycophenolic acid with 2-morpholinoethanol. Best results were achieved by a Candida antarctica lipase B (CAL B) catalyzed transesterification of ethyl mycophenolate in toluene. CAL B showed to selectively transform only the ethyl ester function leaving unreacted the other functional groups present on the substrate. By this way 2-morpholinoethyl mycophenolate was obtained in satisfactory yields from mycophenolic acid (84%).     

The rutin catabolic pathway with special emphasis on quercetinase

The aim of this review is to give a general account on the oxidative microbial degradation of flavonols. Since now 50 years, various research groups have deciphered the way microorganisms aerobically deal with this important class of flavonoids. Flavonols such as rutin and quercetin are abundantly found in vegetal tissues and exudates, and it was thus patent that various microorganisms will bear the enzymatic machinery necessary to cope with these vegetal secondary metabolites. After initial studies focussed on the general metabolic capacity of various microorganisms towards flavonols, the so called rutin catabolic pathway was rapidly established in moulds. Enzymes of the path as well as substrates and products were known at the beginning of the seventies. Then during 30 years, only sporadic studies were focused on this pathway, before a new burst of interest at the beginning of the new century arose with structural, genomic and theorical studies mainly conducted towards quercetinase. This is the goal of this work to relate this 50 years journey at the crossroads of microbiology, biochemistry, genetic and chemistry. Some mention of the potential usefulness of the enzymes of the path as well as micro-organisms bearing the whole rutin catabolic pathway is also discussed.     

An improved procedure for chemospecific acylation of 2-mercaptoethanol by lipase-catalyzed transesterification

Summary Various O-acyl derivatives of 2-mercaptoethanol have been obtained enzymatically by lipase-catalyzed chemospecific esterification reactions of the substrate and several aliphatic carboxylic acid ethyl esters.     

Production of biodiesel by lipase-catalyzed transesterification of vegetable oils: a kinetics study

Kinetics of production of biodiesel by enzymatic methanolysis of vegetable oils using lipase has been investigated. A mathematical model taking into account the mechanism of the methanolysis reaction starting from the vegetable oil as substrate, rather than the free fatty acids, has been developed. The kinetic parameters were estimated by fitting the experimental data of the enzymatic reaction of sunflower oil by two types of lipases, namely, Rhizomucor miehei lipase (RM) immobilized on ion-exchange resins and Thermomyces lanuginosa lipase (TL) immobilized on silica gel. There was a good agreement between the experimental results of the initial rate of reaction and those predicted by the proposed model equations, for both enzymes. From the proposed model equations, the regions where the effect of alcohol inhibition fades, at different substrate concentrations, were identified. The proposed model equation can be used to predict the rate of methanolysis of vegetable oils in a batch or a continuous reactor and to determine the optimal conditions for biodiesel production.