A downstream process with microemulsion extraction for microbial transformation in cloud point system

A downstream process strategy for a whole microbial transformation to produce l-phenylacetylcarbinol (PAC) in a nonionic surfactant Triton X mediated cloud point system was developed. By application of a Winsor I microemulsion, the product and the nonionic surfactant in the microbial transformation broth was separated successfully. Then the nonionic surfactant was recovered with a Winsor II microemulsion. In a single stage Winsor I microemulsion extraction process, the product recovery ratio 76.9% and the nonionic surfactant recovery ratio 66.5% were achieved. A discrete countercurrent extraction operation was also carried out to improve the separation efficiency. Finally, character of the recovery nonionic surfactant was also examined.     

Extractive fermentation in cloud point system for lipase production by Serratia marcescens ECU1010

Extractive microbial fermentation for production of lipase by Serratia marcescens ECU1010 has been carried out in cloud point system. The cloud point system is composed of mixture nonionic surfactants with a ratio of Triton X-114 to Triton X-45 4:1 in aqueous solution. The lipase prefers to partition into the surfactant rich phase (coacervate phase) whereas the cells and other hydrophilic proteins retain in the dilute phase of cloud point system. Thus, a concentration factor 4.2-fold and a purification factor 1.3-fold of the lipase have been achieved in the extractive fermentation process. This is the first report about extractive fermentation of proteins in cloud point system.     

Assessing bioavailability of the solubilization of organic compound in nonionic surfactant micelles by dose–response analysis

It is uncertain in some extent that organic compounds solubilized in micelles of a nonionic surfactant aqueous solution are bioavailable directly by the microbes in an extractive microbial transformation or biodegradation process. In this work, a dose–response method, where a bioequivalence concept is introduced to evaluate the synergic toxicity of the nonionic surfactants and the organic compounds, was applied to analyze the inhibition effect of organic compounds (naphthalene, phenyl ether, 2-phenylethanol, and 1-butanol) in nonionic surfactant Triton X-100 micelle aqueous solutions and Triton X-114 in aqueous solutions forming cloud point systems. Based on the result, a mole solubilization ratio of organic compounds in micelle was also determined, which consisted very well with those of classic semi-equilibrium dialysis experiments. The results exhibit that bioavailability of organic compounds solubilized in micelles to microbial cells is negligible, which provides a guideline for application of nonionic surfactant micelle aqueous solutions or cloud point systems as novel media for microbial transformations or biodegradations.     

A surfactant-coated lipase immobilized in magnetic nanoparticles for multicycle ethyl isovalerate enzymatic production

Gum arabic coated magnetic Fe₃O₄ nanoparticles (GAMNP) were prepared by chemical co-precipitation method and their surface morphology, particle size and presence of polymer-coating was confirmed by various measurements, including transmission electron microscopy (TEM), X-ray diffraction (XRD), thermo gravimetric analysis (TGA), and Fourier transform infra red (FTIR) analysis. Magnetic particles were employed for their potential application as a support material for lipase immobilization. Glutaraldehyde was used as a coupling agent for efficient binding of lipase onto the magnetic carrier. For this purpose, the surface of a Candida rugosa lipase was initially coated with various surfactants, to stabilize enzyme in its open form, and then immobilized on to the support. This immobilized system was used as a biocatalyst for ethyl isovalerate, a flavor ester, production. The influence of various factors such as type of surfactant, optimum temperature and pH requirement, organic solvent used, amount of surfactant in coating lipase and effect of enzyme loadings on the esterification reaction were systematically studied. Different surfactants were used amongst which non-ionic surfactant performed better, showing about 80% esterification yield in 48 h as compared to cationic/anionic surfactants. Enhanced activity due to interfacial activation was observed for immobilized non-ionic surfactant–lipase complex. The immobilized surfactant coated lipase activity was retained after reusing seven times.     

Extractive biodegradation of diphenyl ethers in a cloud point system: Pollutant bioavailability enhancement and surfactant recycling

The biodegradation of diphenyl ethers (DEs) in the environment is limited by their high hydrophobicity. The enhancement of DE bioavailability by a cloud point system (CPS) was investigated in this study. Three CPSs (i.e., Triton X-114, Triton X-114 + Triton X-45, and Brij30 + TMN-3) were tested to promote DE biodegradation. Biocompatibility tests showed that the biodegradation of DE and 4-bromodiphenyl ether (4-BDE) was inhibited by TX-114, unaffected by TX-114 + TX-45, and promoted by Brij30 + TMN-3 over 48 h of cultivation with Cupriavidus basilensis and 4% (w/v) nonionic surfactants. Further optimization with 2% (w/v) Brij30 + TMN-3 yielded residual DE and 4-BDE quantities of 143 and 154 mg/L, respectively, lower than quantities in the control. During degradation, DE content did not decrease in the dilute phase, but sharply decreased in the coacervate phase, indicating that the DEs gradually diffused and transferred from the coacervate phase to the dilute phase for degradation by microbial cells. This behavior also enhanced the bioavailability of DEs in the CPS. By removing the cell-rich dilute phase and adding fresh degradation medium and DE to the coacervate phase, surfactants were successfully recovered and reused twice without affecting DE biodegradation. Results demonstrated that a CPS with 2% (w/v) Brij30 + TMN-3 not only enhanced the bioavailability of DEs, but also decreased the treatment cost through surfactant recycling, which is beneficial for large-scale applications.     

Mixed reverse micelles facilitated downstream processing of lipase involving water‐oil‐water liquid emulsion membrane

Our earlier work for the first time demonstrated that liquid emulsion membrane (LEM) containing reverse micelles could be successfully used for the downstream processing of lipase from Aspergillus niger. In the present work, we have attempted to increase the extraction and purification fold of lipase by using mixed reverse micelles (MRM) consisting of cationic and nonionic surfactants in LEM. It was basically prepared by addition of the internal aqueous phase solution to the organic phase followed by the redispersion of the emulsion in the feed phase containing enzyme, which resulted in globules of water‐oil‐water (WOW) emulsion for the extraction of lipase. The optimum conditions for maximum lipase recovery (100%) and purification fold (17.0‐fold) were CTAB concentration 0.075 M, Tween 80 concentration 0.012 M, at stirring speed of 500 rpm, contact time 15 min, internal aqueous phase pH 7, feed pH 9, KCl concentration 1 M, NaCl concentration 0.1 M, and ratio of membrane emulsion to feed volume 1:1. Incorporation of the nonionic surfactant (e.g., Tween 80) resulted in remarkable improvement in the purification fold (3.1–17.0) of the lipase. LEM containing a mixture of nonionic and cationic surfactants can be successfully used for the enhancement in the activity recovery and purification fold during downstream processing of enzymes/proteins. © 2014 American Institute of Chemical Engineers Biotechnol. Prog., 30:1084–1092, 2014     

Kinetic resolution of rac-alkyl alcohols via lipase-catalyzed enantioselective acylation using succinic anhydride as acylating agent

With succinic anhydride as acylating agent, three commercial lipases – Candida antarctica lipase B (CALB), Pseudomonas cepacia lipase and Pseudomonas fluorescens lipase – were employed in the kinetic resolution of a series of rac-alkyl alcohols: 2-butanol, 2-pentanol, 2-hexanol, 2-heptanol, 2-octanol, 3-hexanol, 3-methyl-2-butanol, 6-methyl-5-heptene-2-ol, 3-methyl-2-cyclohexene-1-ol and 2-methyl-1-pentanol. The most effective tested enzyme, immobilized CALB, was able to resolve most of the alcohols with high enantioselectivity, even higher (with enantiomeric ratios up to 115 and 91, for 3-hexanol and 3-methyl-2-butanol, respectively) than when vinyl acetate was used as the acylating agent. More importantly, the unreacted alcohol and the monoester succinate produced could be easily separated by a simple aqueous base-organic solvent liquid–liquid extraction. Using succinic anhydride as acylating agent and CALB, enantiomerically pure (S)-2-pentanol with 99% ee and (R)-2-pentanol with 95% ee were prepared in gram-scale reactions.     

Whole cell microbial transformation in cloud point system

Cloud point system, consisting of nonionic surfactant in an aqueous solution, has been developed as a novel medium for whole cell microbial transformation. The basic properties of cloud point system including phase separation and solubilization are introduced. The application of cloud point system for extractive microbial transformation is different from that of water-organic solvent two-phase partitioning system or aqueous two-phase system are discussed, which mainly focus on the biocompatibility of microorganism in a cloud point system and a downstream process of microbial transformation in cloud point system with oil-water-surfactant microemulsion liquid-liquid extraction for surfactant recovery and product separation. Finally, examples of whole cell microbial transformation in cloud point systems, especially in situ extraction of moderate polar substrate/product, are also presented.     

Surfactant-modified yeast whole-cell biocatalyst displaying lipase on cell surface for enzymatic production of structured lipids in organic media

The cell surface engineering system, in which functional proteins are genetically displayed on microbial cell surfaces, has recently become a powerful tool for applied biotechnology. Here, we report on the surfactant modification of surface-displayed lipase to improve its performance for enzymatic synthesis reactions. The lipase activities of the surfactant-modified yeast displaying Rhizopus oryzae lipase (ROL) were evaluated in both aqueous and nonaqueous systems. Despite the similar lipase activities of control and surfactant-modified cells in aqueous media, the treatment with nonionic surfactants increased the specific lipase activity of the ROL-displaying yeast in n-hexane. In particular, the Tween 20-modified cells increased the cell surface hydrophobicity significantly among a series of Tween surfactants tested, resulting in 8–30 times higher specific activity in organic solvents with relatively high log P values. The developed cells were successfully used for the enzymatic synthesis of phospholipids and fatty acid methyl esters in n-hexane, whereas the nontreated cells produced a significantly low yield. Our results thus indicate that surfactant modification of the cell surface can enhance the potential of the surface-displayed lipase for bioconversion.     

Solvent effects on the enantioselectivity of the thermophilic lipase QLM in the resolution of (R,S)-2-octanol and (R,S)-2-pentanol

The thermophilic lipase QLM-catalyzed resolution of (R, S)-2-octanol and (R, S)-2-pentanol via transesterification was carried out in various organic solvents, and the solvent effects on the enzyme's enantioselectivity were investigated. A significant negative correlation between the enantiomeric ratio, E, and the size of the solvent molecules was observed. The highest E value, 21, was obtained in the small molecular-sized solvent dichloromethane when (R, S)-2-octanol was resolved with vinyl acetate as acyl donor. Thermodynamic analysis indicated that the difference in activation free energy between the two enantiomers was about 25.5% lower in dichloromethane than in the solvent-free system, and the change in the difference in activation entropy between the enantiomers was the main contributor to the changes in E values with the molecular size of solvents.     

Characteristics of Lipase-Catalyzed Glycerolysis of Triglyceride in AOT-Isooctane Reversed Micelles

Chromobacterium viscosum lipase, solubilized in microemulsion droplets of glycerol containing small amounts of water and stabilized by a surfactant, could catalyze the glycerolysis of triolein. Kinetic analysis of the lipase-catalyzed reaction was possible in the reversed micellar system. Among surfactants and organic solvents tested, bis(2-ethylhexyl)sodiumsulfosuccinate (AOT) and isooctane were respectively most effective, for the glycerolysis of triolein in reversed micelles. Temperature effects, pH profile, K_m,app, and V_max,app were determined. Among various chemical compounds, Fe³⁺, Cu²⁺, and Hg²⁺ inhibited the lipase-catalyzed glycerolysis severely. However, the glycerolysis activity was partially restorable by adding histidine or glycine to the system containing these metal ions. The glycerolysis activity was dependent on water content and maximum activity was obtained at an R value of 1.21. Higher stability of the lipase was obtained in the reversed micellar system.     

Extractive biodecolorization of triphenylmethane dyes in cloud point system by Aeromonas hydrophila DN322p

The biological treatment of triphenylmethane dyes is an important issue. Most microbes have limited practical application because they cannot completely detoxicate these dyes. In this study, the extractive biodecolorization of triphenylmethane dyes by Aeromonas hydrophila DN322p was carried out by introducing the cloud point system. The cloud point system is composed of a mixture of nonionic surfactants (20 g/L) Brij 30 and Tergitol TMN-3 in equal proportions. After the decolorization of crystal violet, a higher wet cell weight was obtained in the cloud point system than that of the control system. Based on the results of thin-layer chromatography, the residual crystal violet and its decolorized product, leuco crystal violet, preferred to partition into the coacervate phase. Therefore, the detoxification of the dilute phase was achieved, which indicated that the dilute phase could be discharged without causing dye pollution. The extractive biodecolorization of three other triphenylmethane dyes was also examined in this system. The decolorization of malachite green and brilliant green was similar to that of crystal violet. Only ethyl violet achieved a poor decolorization rate because DN322p decolorized it via adsorption but did not convert it into its leuco form. This study provides potential application of biological treatment in triphenylmethane dye wastewater.     

K-Na Discrimination by Porous Filters Saturated with Organic Solvents As Expressed by Diffusion Potentials

The permeability ratio of Millipore filters saturated with organic solvents to K and to Na has been studied by measuring the potential difference across these filters. It was found that with n-octanol, toluene, and chloroform the membranes were more permeable to K⁺ than to Na⁺, the degree of discrimination being in inverse proportion to the polarity of the solvent. The dependence of NaCl and KCl diffusion potentials upon the concentration gradients across a filter soaked with about 1:1 toluene/n-butanol solution, could be expressed by the constant field equation, if it is assumed that this layer is 6 to 7 times more permeable to K⁺ than to Na⁺ and that the permeability to Cl^- is negligible. Elevating the fraction of toluene in n-butanol in the separating phase makes it more selective.     

Protein extraction by Winsor‐III microemulsion systems

Proteins (bovine serum albumin (BSA), α‐chymotrypsin, cytochrome c, and lysozyme) were extracted from 0.5 to 2.0 g L^?1 aqueous solution by adding an equal volume of isooctane solution that contained a surfactant mixture (Aerosol‐OT, or AOT, and a 1,3‐dioxolane (or cyclic ketal) alkyl ethoxylate, CK‐2,13‐E_5.6), producing a three‐phase (Winsor‐III) microemulsion with a middle, bicontinuous microemulsion, phase highly concentrated in protein (5–13 g L^?1) and small in volume (12–20% of entire volume). Greater than 90% forward extraction was achieved within a few minutes. Robust W‐III microemulsion systems were formulated at 40°C, or at 25°C by including a surfactant with shorter ethoxylate length, CK‐2,13‐E₃, or 1.5% NaCl (aq). Successful forward extraction correlated with high partitioning of AOT in the middle phase (>95%). The driving force for forward extraction was mainly electrostatic attractions imposed by the anionic surfactant AOT, with the exception of BSA at high ionic strength, which interacted via hydrophobic interactions. Through use of aqueous stripping solutions of high ionic strength (5.0 wt %) and/or pH 12.0 (to negate the electrostatic attractive driving force), cytochrome c and α‐chymotrypsin were back extracted from the middle phase at >75% by mass, with the specific activity of recovered α‐chymotrypsin being >90% of its original value. © 2011 American Institute of Chemical Engineers Biotechnol. Prog., 2011     

微环境对脂肪酶催化拆分外消旋2－辛醇的影响

微环境对脂肪酶催化拆分外消旋２－辛醇的影响　　　　　　　杨红,曹淑桂,韩四平,黄仲丽,杨同书（吉林大学酶工程国家重点实验室,长春１３００２３）手性２－辛醇不仅是制备液晶材料不可缺少的重要手性原料,也是合成具有光学活性的医药和农药的重要手性中间体．本文...     

Design and Evaluation of Self-Microemulsifying Drug Delivery System (SMEDDS) of Tacrolimus

The objective of present investigation was to formulate self-microemulsifying drug delivery systems (SMEDDS) of tacrolimus (FK 506), a poorly water soluble immunosuppressant that exhibits low and erratic bioavailability. Solubility of FK 506 in various oils, surfactants cosurfactants and buffers was determined. Phase diagrams were constructed at different ratios of surfactant/cosurfactant (K _m ) to determine microemulsion existence region. The effect of oil content, pH of aqueous phase, dilution, and incorporation of drug on mean globule size of resulting microemulsions was studied. The optimized SMEDDS formulation was evaluated for in vitro dissolution profile in comparison to pure drug and marketed formulation (Pangraf capsules). The in vivo immunosuppressant activity of FK 506 SMEDDS was evaluated in comparison to Pangraf capsules. Area of o/w microemulsion region in phase diagram was increased with increase in K _m . The SMEDDS yielded microemulsion with globule size less than 25 nm which was not affected by the pH of dilution medium. The SMEDDS was robust to dilution and did not show any phase separation and drug precipitation even after 24 h. Optimized SMEDDS exhibited superior in vitro dissolution profile as compared to pure drug and Pangraf capsules. Furthermore, FK 506 SMEDDS exhibited significantly higher immunosuppressant activity in mice as compared to Pangraf capsules.     

In Situ emulsification and mobilization of gasoline range hydrocarbons using surfactants

In this article the conditions that govern surfactant‐enhanced emulsification and mobilization of petroleum hydrocarbons in soil are reviewed. The effect of soil properties, groundwater constituents, and differing surfactant solutions on the emulsification process is discussed. A constant head soil flushing apparatus used to characterize surfactant‐enhanced mobilization of m‐xylene is described. Data showing the effect of surfactant‐enhanced mobilization on m‐xylene removal efficiency in washed sand is presented. Flushing solutions were used at concentrations from below to well above the critical micelle concentration (CMC) of the surfactants used. Removal efficiencies are shown to vary with surfactant concentration and with surfactant type. Flushing solutions of anionic, nonionic, and anionic/nonionic surfactant mixtures were evaluated.     

Ester Synthesis by a Recombinant Cutinase in Reversed Micelles of a Natural Phospholipid

Fusarium solani pisi recombinant cutinase solubilized in reversed micelles of a nonionic surfactant (phosphatidylcholine) in isooctane was used to catalyze the esterification of fatty acids with 2-butanol. Various parameters affecting the catalytic activity of the microencapsulated cutinase, such as pH, w_o (molar ratio water/surfactant), temperature and substrate concentration were investigated. Maximal specific activity were obtained with w_o=13, at pH 10.7 and 35d`C. The cutinase showed a higher specific activity for short length fatty acids, namely butyric acid. Calculation of the apparent kinetic parameters (k_m and V_max) for the synthesis of butyl butyrate, showed a low apparent affinity of the cutinase in phosphatidylcholine reversed micelles for both substrates.     

Interaction of activating protein and surfactants with human liver hexosaminidase A and GM2 ganglioside

The effects of surfactants on the human liver hexosaminidase A-catalysed hydrolysis of G_m2 ganglioside were assessed. Some non-ionic surfactants, including Triton X-100 and Cutscum, and some anionic surfactants, including sodium taurocholate, sodium dodecyl sulphate, phosphatidylinositol and N-dodecylsarcosinate, were able to replace the hexosaminidase A-activator protein [Hechtman (1977) Can. J. Biochem. 55, 315–324; Hechtman & Leblanc (1977) Biochem. J. 167, 693–701) and also stimulated the enzymic hydrolysis of substrate in the presence of saturating concentrations of activator. Other non-ionic surfactants, such as Tween 80, Brij 35 and Nonidet P40, and anionic surfactants, such as phosphatidylethanolamine, did not enhance enzymic hydrolysis of G_m2 ganglioside and inhibited hydrolysis in the presence of activator. The concentration of surfactants at which micelles form was determined by measurements of the minimum surface-tension values of reaction mixtures containing a series of concentrations of surfactant. In the case of Triton X-100, Cutscum, sodium taurocholate, N-dodecylsarcosinate and other surfactants the concentration range at which stimulation of enzymic activity occurs correlates well with the critical micellar concentration. None of the surfactants tested affected the rate of hexosaminidase A-catalysed hydrolysis of 4-methylumbelliferyl N-acetyl-β-d-glucopyranoside. Both activator and surfactants that stimulate hydrolysis of G_m2 ganglioside decrease the K_m for G_m2 ganglioside. Inhibitory surfactants are competitive with the activator protein. Evidence for a direct interaction between surfactants and G_m2 ganglioside was obtained by comparing gel-filtration profiles of ³H-labelled G_M2 ganglioside in the presence and absence of surfactants. The results are discussed in terms of a model wherein a mixed micelle of surfactant or activator and G_M2 ganglioside is the preferred substrate for enzymic hydrolysis.     

Feasibility of using water-immiscible organic solvents in biological waste-gas treatment

In order to conclude about the feasibility of using water-immiscible organic solvents in biological waste-gas treatment, a theoretical study was done in which different types of organic-solvent-containing systems are compared with systems where the pollutant is transferred directly to the water phase. For each system the total equipment volume needed to remove 99% of a pollutant from a waste-gas stream is calculated. Three different pollutants with a different solubility in water are considered: Hexane (m _gw =71), dichloromethane (m _gw =0.1) and acetone (m _gw =0.0016), withm _gw the partition coefficient (kg/m³ gas/kg/m³ water) of the pollutant between the gas and the water phase. From the results it is concluded that the use of organic solvents is only advantageous in case the specific area for mass transfer between solvent and water is large enough to compensate for the additional transport resistance introduced by the solvent, and secondly if the solvent shows a sufficiently high affinity for the pollutants.