Theoretical development and performance evaluation for extractive fermentation using multiple extractants

Mathematical formulation was made for the performance evaluation of extractive fermentation using multiple solvents. Two types of solvent-supplying strategies were considered. One is to add multiple solvents simultaneously and the product is removed at one time. Another is to add them one by one consecutively. Computer simulation was made for batch, fed-batch, and repeated fed-batch operation of acetone-butanol fermentation to show the power of the approach. The result shows that the significant performance improvement in terms of the productivity and the product concentration is expected when two extractants such as oleyl alcohol and benzyl benzoate are used as compared with the case of using only one solvent.     

In-situ recovery of butanol during fermentation

End product inhibition can be reduced by the in situ removal of inhibitory fermentation products as they form. Extractive fermentation, in which an immiscible organic solvent is added to the fermentor in order to extract inhibitory products, was applied to the acetone-butanol fermentation. Six solvents or solvent mixtures were tested in batch extractive fermentations: kerosene, 30 wt% tetradecanol in kerosene, 50 wt% dodecanol in kerosene, oleyl alcohol, 50 wt% oleyl alcohol in a decane fraction and 50 wt% oleyl alcohol in benzyl benzoate. The best results were obtained with oleyl alcohol or a mixture of oleyl alcohol and benzyl benzoate. In normal batch fermentation of Clostridium acetobutylicum, glucose consumption is limited to about 80 kg/m³ due to the accumulation of butanol in the broth. In extractive fermentation using oleyl alcohol or a mixture of oleyl alcohol and benzyl benzoate, over 100 kg/m³ of glucose can be fermented. Removal of butanol from the broth as it formed also increased the rate of butanol production. Maximum volumetric butanol productivity was increased by as much as 60% in extractive fermentation compared to batch fermentation. Butanol productivities obtained in extractive fermentation compare favorably with other in situ product removal fermentations.     

Efficient kinetic resolution of dl-menthol by lipase-catalyzed enantioselective esterification with acid anhydride in fed-batch reactor

Acid anhydrides were used as highly reactive and non-water-producing acyl donors for hydrolase-catalyzed enantioselective esterification. Efficient kinetic resolution of dl-menthol has been achieved via lipase-catalyzed enantioselective esterification in cyclohexane when propionic anhydride as an acyl donor was continuously fed into a reactor containing dl-menthol and Candida cylindracea lipase OF 360, while a high concentration of the acid anhydride in a batch reaction system with a dehydrated organic solvent did not facilitate the reaction, because water necessary for the enzyme function was consumed by the competing hydrolysis of the anhydride catalyzed by the same enzyme. The efficiency of this fed-batch reaction system using acid anhydride was higher and the enzyme stability in repeated use was much better than those of conventional batch and fed-batch reaction systems using propionic acid as an acyl donor. The optical purity (more than 98% e.e.) of the l-menthyl ester produced in the fed-batch system using the anhydride was comparable to that in the system using the corresponding acid. *** DIRECT SUPPORT *** AG903062 00002     

Lipase catalyzed synthesis of benzyl acetate in solvent-free medium using vinyl acetate as acyl donor

Use of vinyl acetate as acyl donor in transesterification of benzyl alcohol catalyzed by a commercially available lipase (Lipozyme RM IM) gave 100% conversion in 10 min. The excess acyl donor and the enzyme could be recovered and reused. Unlike the chemical catalytic processes, it produced no undesirable side product.     

Biocatalytic preparation of acylated derivatives of flavonoid glycosides enhances their antioxidant and antimicrobial activity

Enzymatic synthesis of acylated derivatives of a monosaccharidic flavonoid chrysoeriol-7-O-beta-D-(3'-E-p-coumaroyl)-glucopyranoside as well as of a disaccharidic flavonoid chrysoeriol-7-[6'-O-acetyl-beta-D-allosyl-(1-->2)-beta-D-glucopyranoside], isolated from Greek endemic plants, was performed using an immobilized Candida antarctica lipase in non-toxic organic solvents. The influence of the reaction parameters such as the molar ratio of acyl donor to flavonoid, as well as the nature of the acyl donor, on the performance of the biocatalytic process was pointed out using the acylation of naringin as a model reaction. With vinyl laurate as acyl donor, the highest conversion was observed at relatively high molar ratio (>or=10), using acetone as solvent. Lipase exhibits specificity towards primary alcohol of the glucose moiety of both flavonoid glycosides. The introduction of an acyl group into glucosylated flavonoids significantly improved their antioxidant activity towards both LDL and serum model in vitro. Furthermore, the acylated derivative of disaccharidic flavonoid increased its antimicrobial activity against two Gram-positive bacteria.     

Different enzyme requirements for the synthesis of biodiesel: Novozym 435 and Lipozyme TL IM

Enzymatic syntheses of biodiesel via alcoholysis of different vegetable oils (sunflower, borage, olive and soybean) have been studied. Loss of lipase activity induced by the nucleophile is greater with methanol than with ethanol, and is greater for Lipozyme TL IM than for Novozym 435. The optimum volume of ethanol depends on the loading of solid biocatalyst and is higher for preparations of Novozym 435 than for Lipozyme TL IM. Maximum rates were obtained with Lipozyme TL IM, for a molar ratio of alcohol to FA residues of 0.33. By contrast, Novozym 435 requires at least a 2:1 ratio. Alcoholysis of the vegetable oils is faster with Lipozyme TL IM than with Novozym 435. Use of a high loading of Novozym 435 (50% w/w) and a large molar excess of ethanol are required to obtain an initial rate similar to that obtained with Lipozyme TL IM at a lower enzyme loading (10% w/w) and an equimolar ratio of ethanol and FA residues. Novozym 435 produces quantitative conversions in only 7h at 25 degrees C, but complete conversions are not obtained with Lipozyme TL IM. Three stage stepwise addition of ethanol yields 84% conversion to ethyl esters for Lipozyme TL IM. Hence use of Novozym 435 is preferred. After nine cycles in a batch reactor Novozym 435 retained 85% of its initial activity.     

Transesterification of primary and secondary alcohols using Pseudomonas aeruginosa lipase

Lipases of a newly isolated Pseduomonas aeruginosa MTCC 5113 were assessed for transesterification of benzyl alcohol and vinyl acetate to produce the flavoring agent benzyl acetate. Crude lipase preparations that minimized the cost of the biocatalyst, achieved benzyl alcohol conversion of 89% within 3h at 30 degrees C. In contrast, purified and expensive commercially available lipases of Candida antarctica and porcine pancreas achieved much lower conversions at 80% and 15%, respectively. A well-mixed ( approximately 800 rev.min(-1)) batch reactor having the aqueous phase finely dispersed in heptane was used in these studies. Benzyl alcohol conversion was maximal when the enzyme-containing aqueous phase constituted about 50% of the total reactor volume. Use of solvents such as hexane, benzene, toluene and dimethyl sulfoxide reduced conversion compared with the use of heptane.     

Improved high-pressure enzymatic biodiesel batch synthesis in near-critical carbon dioxide

The enzymatic synthesis of biodiesel by a high-pressure semi-continuous process in near-critical carbon dioxide (NcCO(2)) was studied. Biodiesel synthesis was evaluated in both batch and semi-continuous systems to develop an effective process. Batch processing demonstrated the advantageous properties of NcCO(2) as an alternative reaction medium. Three immobilized lipases (Novozym 435, Lipozyme RM IM, and Lipozyme TL IM from Novozymes) were tested, with Lipozyme TL IM the most effective, showing the highest conversion. Biodiesel conversion from several edible and non-edible oil feedstocks reached >92%. Higher conversion (99.0%) was obtained in a shorter time by employing repeated batch processes with optimized conditions: 44.3 g (500 mM) canola oil, a substrate molar ratio (methanol:oil) of 3:1, an enzyme loading of 20 wt% (of the oil used), at 30 °C, 100 bar, and 300 rpm agitation. The enzyme maintained 80.2% of its initial stability after being reused eight times. These results suggest that this method produces biodiesel energy-efficiently and environment-friendly.     

Lipase-catalyzed esterification of hydrophilic diols in organic solvents

Summary The direct, lipase-catalyzed esterification of hydrophilic diols in organic solvents was achieved by first adsorbing the hydrophilic, solvent immiscible substrate onto a solid support with high internal surface, namely silica gel and reacting the solid mixture with fatty acid vinyl esters in an appropriate organic solvent and in presence of an immobilized lipase fromMucor miehei (Lipozyme). Quantitative conversions of the acyl donors and very high reaction rates were observed in these transformations. Furthermore, mono- or diesters of these diols could be selectively produced by this method.     

Lipase-catalyzed regioselective synthesis of steryl (6′-<Emphasis Type="Italic">O</Emphasis>-acyl)glucosides

The regioselective acylation of cholesteryl β-d-glucoside, at the C-6 of the glucose moiety, was achieved using microbial lipases in organic solvents. With palmitic acid as an acyl donor 81 or 63% conversions of cholesteryl glucoside to its 6′-O-palmitoyl derivative were obtained using Candida antarctica or Rhizomucor miehei enzymes, respectively. High yields (64–92%) were also obtained with fatty acids 6:0–22:0 and 16:1 (n-7). The synthesis of cholesteryl (6′-O-palmitoyl)glucoside was also achieved via transesterification, using mono-, di- and tri-palmitoylglycerols or methyl and ethyl palmitate as acyl sources. With R. miehei lipase transesterification between methyl palmitate (80 mM) and cholesteryl glucoside (1 mM) proceeded after 24 h with a nearly quantitative yield (97%).     

Lipase-catalyzed synthesis and antibacterial activity of N-vanillylnonanamide

N-vanillylnonanamide (VAN) was successfully synthesized from vanillylamine hydrochloride by enzymatic catalysis in supercritical carbon dioxide (SC–CO₂). Five commercial lipases, Novozyme 435, Lipozyme IM, Amano PS, Amano G and Sigma Candida cylindracea type VII, as biocatalysts for VAN synthesis were compared. Lipozyme IM exhibited best yields of tested lipases. Various parameters such as time, temperature, pressure and vanillylamine hydrochloride/nonanoic anhydride ratio that influenced the reaction were investigated. Nonanoic anhydride showed the best acyl donor of the employed substrates. An amidation yield of 40% was obtained when nonanoic anhydride and Lipozyme IM were used at 170 bar and 50 °C for 23 h in SC–CO₂. Besides, addition of 2 mM divalent salts (CuCl₂ and ZnCl₂) significantly increased 11–23% yield of the VAN. The enzyme operational stability suggested that Lipozyme IM maintained over 50 °C of the initial activity for the synthesis of VAN after reuse for 69 h. Furthermore, in vitro, VAN behaved as a potential antibacterial against Escherichia coli.     

Enzymatic resolution of 2-aryloxy-1-propanols via lipase-catalyzed enantioselective acylation using acid anhydrides as acyl donors

Pseudomonas sp. lipase-catalyzed enantioselective acylation procedure using acid anhydrides as acyl donors was exploited for the resolution of 2-aryloxy-1-propanols carrying different substituents on the benzene ring. These primary alcohols, which belong to primary alcohols with an oxygen atom at the stereocenter, were resolved generally with moderate to good enantioselectivity (E of up to 55) through the acylation with hexanoic anhydride in diisopropyl ether at 25 °C in a short reaction time. With the alcohol substrate, which gave a low enantioselectivity in the acylation at ordinary temperature, the selectivity proved to be enhanced by conducting the reaction at low temperature (−10 °C). By this acylation procedure employing the acid anhydride, enantiomerically pure (R)-2-phenoxy-1-propanol was prepared in a gram-scale reaction.     

Anaerobic degradation of toluene in denitrifying Pseudomonas sp.: indication for toluene methylhydroxylation and benzoyl-CoA as central aromatic intermediate

The anaerobic degradation of toluene has been studied with whole cells and by measuring enzyme activities. Cultures of Pseudomonas strain K 172 were grown in mineral medium up to a cell density of 0.5 g of dry cells per liter in fed-batch culture with toluene and nitrate as the sole carbon and energy sources. A molar growth yield of 57 g of cell dry matter formed per mol toluene totally consumed was determined. The mean generation time was 24 h. The redox balance between toluene consumed (oxidation and cell material synthesis) and nitrate consumed (reduction to nitrogen gas and assimilation as NH₃) was 77% of expectation if toluene was completely oxidized; this indicated that the major amount of toluene was mineralized to CO₂. It was tested whether the initial reaction in anaerobic toluene degradation was a carboxylation or a dehydrogenation (anaerobic hydroxylation); the hypothetical carboxylated or hydroxylated intermediates were tested with whole cells applying the method of simultanous adaptation: cells pregrown on toluene degraded benzyl alcohol, benzaldehyde, and benzoic acid without lag, 4-hydroxybenzoate and p-cresol with a 90 min lag phase and phenylacetate after a 200 min lag phase. The cells were not at all adapted to degrade 2-methylbenzoate, 4-methylbenzoate, o-cresol, and m-cresol, nor did these compounds support growth within a few days after inoculation with cells grown on toluene. In extracts of cells anaerobically grown on toluene, benzyl alcohol dehydrogenase, benzaldehyde dehydrogenase, and benzoyl-CoA synthetase (AMP forming) activities were present. The data (1) conclusively show anaerobic growth of a pure culture on tolucne; (2) suggest that toluene is anaerobically degraded via benzoyl-CoA; (3) imply that water functions as the source of the hydroxyl group in a toluene methylhydroxylase reaction.     

High yield lipase-catalyzed synthesis of Engkabang fat esters for the cosmetic industry

Engkabang fat esters were produced via alcoholysis reaction between Engkabang fat and oleyl alcohol, catalyzed by Lipozyme RM IM. The reaction was carried out in a 500 ml Stirred tank reactor using heptane and hexane as solvents. Response surface methodology (RSM) based on a four-factor-five-level Central composite design (CCD) was applied to evaluate the effects of synthesis parameters, namely temperature, substrate molar ratio (oleyl alcohol: Engkabang fat), enzyme amount and impeller speed. The optimum yields of 96.2% and 91.4% were obtained for heptane and hexane at the optimum temperature of 53.9 °C, impeller speeds of 309.5 and 309.0 rpm, enzyme amounts of 4.82 and 5.65 g and substrate molar ratios of 2.94 and 3.39:1, respectively. The actual yields obtained compared well with the predicted values of 100.0% and 91.5%, respectively. Meanwhile, the properties of the esters show that they are suitable to be used as ingredient for cosmetic applications.     

Regulation of growth of Acinetobacter calcoaceticus NCIB8250 on L-mandelate in batch culture.

Batch culture of Acinetobacter calcoaceticus in L-mandelate- or phenylglyoxylate-salts medium showed an unusual non-exponential pattern unless the inoculum had been grown on benzyl alcohol. There were transient accumulations of benzaldehyde and benzyl alcohol caused by the limitation of L-mandelate oxidation by low activities of benzaldehyde dehydrogenase and the diversion of reducing power to the formation of benzyl alcohol. In vivo enzymic activities were estimated from patterns of substrate utilization in batch cultures containing pairs of substrates. When bacteria previously grown in L-mandelate-salts medium were inoculated into media containing L-mandelate and a second carbon source, metabolism of L-mandelate was arithmetical in the presence of benzoate, catechol or succinate, but accelerated on exhaustion of the second substrate. This indicated repression of the enzymes involved in L-mandelate oxidation. Inoculation of bacteria grown in benzoate-salts medium into medium containing L-mandelate and benzoate gave diauxie with initial utilization of benzoate. Similar experiments showed that benzoate oxidation was not repressed by catechol and only partially repressed by succinate. Measurement of L-mandelate dehydrogenase, phenylglyoxylate carboxy-lyase and benzaldehyde dehydrogenase I in bacterial extracts showed no evidence for feedback inhibition by intermediates of the pathway. The rates of L-mandelate and benzoate utilization by bacterial suspensions were inhibited by succinate and catechol but not by other intermediates of the pathway.     

Linear and cyclic ester Oligomers of succinic acid and 1,4-butanediol: Biocatalytic synthesis and characterization

Abstract

The lipase-catalyzed synthesis of cyclic ester oligomers from non-activated succinic acid (A) and 1,4-butanediol (B) in the presence of immobilized Candida antarctica lipase B was investigated. Batch and pulse fed-batch systems were implemented to increase the formation of cyclic ester products. The substrate conversions after 24 h were 86% and 95% under batch and fed-batch operation, respectively and the product of the reaction was, for both systems, a mixture of cyclic (CEOs) and linear (LEOs) ester oligomers. Fed-batch operation afforded a product containing 71% cyclic ester oligomers (CEOs) as compared with only 52% CEOs in batch operation. Cyclic ester oligomers accumulated as the reaction progressed, with the dimer CEO₁ the most predominant product (i.e. 50% of the total products formed in fed-batch operation). The pulse fed-batch operation system was superior to the batch operation not only because higher substrate conversion and more CEOs were obtained, but also because it resulted in products with a higher degree of polymerization (DP up to 7). Cyclic ester oligomers are produced from the early stage of the reaction simultaneously with the linear ester oligomers by a ring-closure reaction on the active site of the enzyme, and not as a result of ring-chain equilibria.     

Enzymatic production of linalool esters in organic and solvent-free system

This work investigated the influence of temperature, enzyme concentration, substrates molar ratio, in the absence and presence of organic solvent, at two molar ratios of the substrates on the enzymatic production of linalil esters using the immobilized lipase Novozym 435 as catalyst, different acids and linalool and Ho-Sho essential oil as substrates. The best reaction conversion was obtained at the highest temperature (70 °C), for both solvent free (3.81%) and with solvent addition (2.25%), for a solvent to substrates molar ratio of 2:1, enzyme concentration of 5 wt% and acid to alcohol molar ratio of 1:1. The reaction kinetics revealed that Ho-Sho essential oil afforded the greatest conversions when compared with pure linalool. Higher linalil esters production were achieved after 10 h reaction (5.58%) in 2:1 solvent to substrates molar ratio, with enzyme concentration of 5 wt%, at 70 °C and anhydride to alcohol molar ratio of 1:1 using Ho-Sho essential oil as substrate.     

Floral scent of Canada thistle and its potential as a generic insect attractant

The flowers of Canada thistle, Cirsium arvense (L.), attract a wide range of insects, including pollinators and herbivorous species. This attraction is primarily mediated by floral odor, which offers potential for developing generic insect attractants based on odor. In this study, we have analyzed the chemical composition of the volatiles produced by Canada thistle flowers. Nineteen floral compounds were identified in the headspace, including phenylacetaldehyde (55%), methyl salicylate (14%), dimethyl salicylate (8%), pyranoid linalool oxide (4.5%), and benzaldehyde (3.5%). Other minor compounds include benzyl alcohol, methylbenzoate, linalool, phenylethyl alcohol, furanoid linalool oxide, p-anisaldehyde, 2,6-dimethyl-1,3,5,7-octatetraene, benzylacetate, benzyl tiglate, (E,E)-alpha-farnesene, benzyl benzoate, isopropyl myristate, and 2-phenylethyl ester benzoic acid. The relative attractiveness of various doses of the main floral volatile compound phenylacetaldehyde (i.e., 10, 100, 200, and 400 mg) was tested for insect attraction. Both the total catch and the biodiversity of insect species trapped increased as the loading of phenylacetaldehyde increased. Volatiles were chosen from the odors from the flowers of Canada thistle and formulated and tested in the field. An 11-component blend was the most attractive of several floral blends tested. These findings indicate that chemical components of flower odors of Canada thistle can serve as a generic insect attractant for monitoring of invasive pest species.     

Enzyme catalyzed synthesis of some vinyl drug esters in organic medium

A series of vinyl drug esters was synthesized using acyclovir and chloramphenicol with different carbon chain length acyl donors by alkaline protease from Bacillus subtilis and Lipozyme respectively, in non-aqueous medium. The corresponding vinyl drug derivatives were confirmed by nuclear magnetic resonance and infrared spectrometry. The influences of different organic solvents, reaction time, temperature, and content of water on synthesis of vinyl chloramphenicol esters were studied.     

New segment synthesis of alpha-inhibin-92 by the acyl disulfide method

The thiocarboxyl group reacts with diaryl disulfides to give an unsymmetrical acyl disulfide in dimethylformamide (DMF) and a symmetrical diacyl disulfide in aqueous DMF. Both acyl disulfides react with the alpha-amino group to form the peptide bond. The method was used in a new segment synthesis of alpha-inhibin-92 (alpha-IB-92) with use of 2,2'-dipyridyl disulfide as activator. Thiocarboxyl peptides were synthesized by the solid-phase method on 4-[alpha-(Boc-Gly-S)benzyl]phenoxyacetamidomethyl-resin. The segments alpha-IB-92-(1-34)SH (I), Msc-alpha-IB-92-(35-65)SH (II), Msc-alpha-IB-92(66-92)OH (III), and Msc-alpha-IB-92-(35-92)OH (VI) were prepared in yields of 33, 36, 41, and 25%, respectively, with use of crystalline symmetrical anhydrides in double and triple coupling protocols. Segments I, II, and III were used in a 3-segment synthesis of alpha-IB-92 with an overall yield based on starting resin of about 8% while a 2-segment synthesis using I and IV gave 11%. An all stepwise synthesis of alpha-IB-92 gave 4.5%.