Spatially resolved in situ determination of reaction progress using microfluidic systems and FT-IR spectroscopy as a tool for biocatalytic process development.

A concept for the determination of concentrations in microchannels using FT-IR spectroscopy in transmission is presented. The fundamental idea of spatially resolved measurements along several measuring points was implemented in a single-channel microreactor. Compared to existing microreactor setups for the analysis of fast chemical reactions or mixing processes, the presented concept enables longer residence times at appropriate resolution. Once steady-state conditions were reached in the reactor, mid-infrared spectra were collected at different locations. Information throughout the considered conversion range is available, which is of great importance to analyze inhibitory effects, next to the kinetic constants (vmax and KM). Therefore, this technology enables a rapid screening of (bio-)catalysts, substrate specificity and process conditions. In particular, the analysis of real substrates instead of model substrates and the possibility to follow side reactions and follow-up reactions during enzymatic catalysis open a broad field of application.

Pseudomonas aeruginosa biofilm growth inhibition on medical plastic materials by immobilized esterases and acylase.

Biofilms are matrix-encapsulated cell aggregates that cause problems in technical and health-related areas; for example, 65 % of all human infections are biofilm associated. This is mainly due to their ameliorated resistance against antimicrobials and immune systems. Pseudomonas aeruginosa, a biofilm-forming organism, is commonly responsible for nosocomial infections. Biofilm development is partly mediated by signal molecules, such as acyl-homoserine lactones (AHLs) in Gram-negative bacteria. We applied horse liver esterase, porcine kidney acylase, and porcine liver esterase; these can hydrolyze AHLs, thereby inhibiting biofilm formation. As biofilm infections are often related to foreign material introduced into the human body, we immobilized the enzymes on medical plastic materials. Biofilm formation was quantified by Crystal Violet staining and confocal laser scanning microscopy, revealing up to 97 % (on silicone), 54 % (on polyvinyl chloride), and 77 % (on polyurethane) reduced biomass after 68 h growth.

Novel µ-membrane module for online determination of the free fatty acid content in the dispersed phase of oil-in-water emulsions.

Monitoring the dispersed phase of an oil-in-water (O-W) emulsion by means of Fourier transform infrared (FTIR) spectroscopy is a challenging task, restricted to the continuous phase that is in contact with the FTIR probe. Nonetheless, real-time measurement and kinetic analysis by FTIR, including analysis of the dispersed, often non-polar phase containing substrates and/or products, is desirable. Enzymatic hydrolysis of sunflower oil was performed in an O-W emulsion. After separation of the oil phase by use of a newly developed µ-membrane module, infrared spectra were collected using an attenuated total reflectance (ATR) cell. Different chemometric models were calibrated using the partial least squares (PLS) algorithm. Online application of a chemometric model based on the FTIR spectra enabled real-time monitoring of free fatty acid concentrations in the oil phase.

Strategies for reliable and improved large-scale production of Pyrococcus furiosus with integrated purification of hydrogenase I.

The hyperthermophilic archaeon Pyrococcus furiosus is an interesting organism for research and application, especially owing to its unique NADPH-dependent hydrogenase I. However, mass production of P. furiosus through fermentation is susceptible to fault because of its sensitivity to oxygen, a short exponential and stationary phase and a rapid cell lysis in typical cultivation process. In this study, significant improvement for pilot plant scale production processes for P. furiosus biomass was made by investigations of the fermentation process with subsequent hydrogenase I enzyme purification. Scale-up in a 300-L stirred tank bioreactor was successfully achieved. A repeated-batch cultivation process with high reproducibility and productivity was realized. Furthermore, the enzyme hydrogenase I was purified, and its activity tested and verified. The improvements in this production process for the production of large amount of P. furiosus biomass and hydrogenase I have been achieved, especially by successfully implementing the following key measures and steps: unsterile cultivation setup, skipping typical intermediate preculture and inoculation steps, accelerating the cultivation process by defining an optimal state of the inoculation, optimal time point of biomass harvesting and finally by choosing a one-step purification procedure for enzyme recovery.

Evaluation of immobilized enzymes for industrial applications.

In contrast to the application of soluble enzymes in industry, immobilized enzymes often offer advantages in view of stability, volume specific biocatalyst loading, recyclability as well as simplified downstream processing. In this tutorial review the focus is set on the evaluation of immobilized enzymes in respect to mass transport limitations, immobilization yield and stability, to enable industrial applications.

In situ microscopy for in-line monitoring of the enzymatic hydrolysis of cellulose.

A new in-line method for the monitoring of enzymatic hydrolysis of cellulose is described. Using a new in situ microscope prototype, the noninvasive determination of particle size distributions was possible. For the automated analysis of the acquired images, a new processing algorithm called CelluloseAnalyzer was developed. It enabled tracking of the number of particles and moreover allowed monitoring of the proportions of particle size fractions during the course of enzymatic hydrolysis reactions. Using this technique, significant differences between hydrolysis with endoglucanases and cellulase mixtures were observed. Furthermore, the in situ microscopy results were compared with results from off-line measurements with laser diffraction spectroscopy and gel permeation chromatography.

A chemo-enzymatic route to synthesize (S)-γ-valerolactone from levulinic acid.

Levulinic acid is a feasible platform chemical derived from acid-catalyzed hydrolysis of lignocellulose. The conversion of this substrate to (S)-γ-valerolactone ((S)-GVL) was investigated in a chemo-enzymatic reaction sequence that benefits from mild reaction conditions and excellent enantiomeric excess of the desired (S)-GVL. For that purpose, levulinic acid was chemically esterified over the ion exchange resin Amberlyst 15 to yield ethyl levulinate (LaOEt). The keto ester was successfully reduced by (S)-specific carbonyl reductase from Candida parapsilosis (CPCR2) in a substrate-coupled cofactor regeneration system utilizing isopropanol as cosubstrate. In classical batch experiments, a maximum conversion of 95 % was achieved using a 20-fold excess of isopropanol. Continuous reduction of LaOEt was carried out for 24 h, and a productivity of more than 5 mg (S)-ethyl-4-hydroxypentanoate (4HPOEt) per µg CPCR2 was achieved. Afterwards (S)-4HPOEt (>99%ee) was substituted to lipase-catalyzed lactonization using immobilized lipase B from Candida antarctica to yield (S)-GVL in 90 % overall yield and >99%ee.

Kinetic investigation of a solvent-free, chemoenzymatic reaction sequence towards enantioselective synthesis of a ß-amino acid ester.

A solvent-free, chemoenzymatic reaction sequence for the enantioselective synthesis of ß-amino acid esters has been kinetically and thermodynamically characterized. The coupled sequence comprises a thermal aza-Michael addition of cheap starting materials and a lipase catalyzed aminolysis for the kinetic resolution of the racemic ester. Excellent ee values of >99% were obtained for the ß-amino acid ester at 60% conversion. Kinetic constants for the aza-Michael addition were obtained by straightforward numerical integration of second-order rate equations and nonlinear fitting of the progress curves. A different strategy had to be devised for the biocatalytic reaction. Initially, a simplified Michaelis-Menten model including product inhibition was developed for the reaction running in THF as an organic solvent. Activity based parameters were used instead of concentrations in order to facilitate the transfer of the kinetic model to the solvent-free system. Observed solvent effects not accounted for by the use of thermodynamic activities were incorporated into the kinetic model. Enzyme deactivation was observed to depend on the ratio of the applied substrates and also included in the kinetic model. The developed simple model is in very good agreement with the experimental data and allows the simulation and optimization of the solvent-free process.

Simultaneous determination of mono-, di-, and triglycerides in multiphase systems by online Fourier transform infrared spectroscopy.

Glycerides are of significant value for industry as ingredients with different purposes in food or cosmetics. The analysis of glycerides is mainly performed by gas chromatography (GC) or high-pressure liquid chromatography (HPLC), which demonstrate limitations in dealing with multiphase systems. In this article, an in situ differentiation between mono-, di-, and triglycerides in multiphase systems by Fourier transform infrared (FT-IR) spectroscopy is demonstrated. The enzymatic esterification of glycerol with lauric acid was analyzed as a model system. The reaction was carried out in a bubble column reactor containing four phases (two liquid phases of glycerol and lauric acid, air as gaseous phase, and a heterogeneous catalyst as solid phase). As a feasibility study, a chemometric model was generated for the pure components only. The quantities of lauric acid and the three products (mono-, di-, and trilaurin) were simultaneously determined over the course of the reaction with acceptable errors (1.8-12.5%) with regard to the calibration effort. This technology has the potential to give accurate results, particularly in unstable emulsion systems containing fats, oils, or emulsifiers, which are currently afflicted by analytical errors caused by the challenge of accurate sampling.

Dissolving carbon dioxide in high viscous substrates to accelerate biocatalytic reactions.

Solvent free biotransformation of polyglycerol-3 and lauric acid yields polyglycerol-3-laurate and water. This conversion can be catalyzed by Novozym 435. However, the performance is limited by the viscosity of polyglycerol as well as of polyglycerol-3-laurate. A decrease of viscosity by increasing reaction temperature is only possible in a certain temperature range because of the limited stability of the applied enzyme. By dissolving high dense carbon dioxide into the reaction system the viscosity could be reduced, keeping the temperature at an acceptable level at the same time. Thus the reaction rate was increased by a factor of 4 while working at a pressure of 280 bar and 60°C.

Online monitoring of biotransformations in high viscous multiphase systems by means of FT-IR and chemometrics.

In unstable emulsion systems, the determination of concentrations is a challenge. The use of standard methods like GC, HPLC, or titration is highly inaccurate and makes the acquisition of precise data for these systems complex. In addition, the handicap of high viscosity often comes into play. To overcome these fundamental limitations, the online FT-IR technique was identified in combination with chemometric modeling in order to improve accuracy. The reactor type used in this study is a bubble column reactor with up to four dispersed phases (solid catalyst, two liquid immiscible substrates, and a gaseous phase). The investigated reactions are solvent free enzymatic esterifications yielding myristyl myristate (10 mPa s) and high viscous polyglycerol-3-laurate (300-1500 mPa s), representative industrial products for cosmetic applications. For both reactions, chemometric models were successfully set up and reproducibly applied in the prediction of progress curves of a new set of experiments. This allows the automated determination of sensitive kinetic and thermodynamic data as well as reaction velocities in high viscous multiphase (bio)chemical systems.

Improvement of the Process Stability of Arylmalonate Decarboxylase by Immobilization for Biocatalytic Profen Synthesis.

The enzyme arylmalonate decarboxylase (AMDase) enables the selective synthesis of enantiopure (S)-arylpropinates in a simple single-step decarboxylation of dicarboxylic acid precursors. However, the poor enzyme stability with a half-life time of about 1.2 h under process conditions is a serious limitation of the productivity, which results in a need for high catalyst loads. By immobilization on an amino C2 acrylate carrier the operational stability of the (S)-selective AMDase variant G74C/M159L/C188G/V43I/A125P/V156L was increased to a half-life of about 8.6 days, which represents a 158-fold improvement. Further optimization was achieved by simple immobilization of the cell lysate to eliminate the cost- and time intensive enzyme purification step.

Process development for oxidations of hydrophobic compounds applying cytochrome P450 monooxygenases in-vitro.

Cytochrome P450 monooxygenases are a unique family of enzymes that are able to catalyze regio- and stereospecific oxidations for a broad substrate range. However, due to limited enzyme activities and stabilities, hydrophobicity of substrates, as well as the necessity of a continuous electron and oxygen supply the implementation of P450s for industrial processes remains challenging. Aim of this study was to point out key aspects for the development of an efficient synthesis concept for cytochrome P450 catalyzed oxidations. In order to regenerate the natural cofactor NADPH, a glucose dehydrogenase was applied. The low water soluble terpene α-ionone was used as substrate for the model reaction system. The studies reveal that an addition of surfactants in combination with low volumetric amounts of co-solvent can significantly increase substrate availability and reaction rates. Furthermore, these additives facilitated a reliable sampling procedure during the process. Another key factor for the process design was the oxygen supply. Based on various investigations, a bubble-aerated stirred tank reactor in batch mode represents a promising reactor concept for P450 oxidations. Main restriction of the investigated reaction system was the low process stability of the P450 monooxygenase, characterized by maximum total turnover numbers of ∼4100molα-ionone/molP450.

Building blocks.

This contribution illustrates the versatility of fundamental approaches in industrial biotransformations. The applicability of biotechnology in organic synthesis on an industrial scale is discussed, followed by an overview of historical development and future progress. This chapter depicts three different approaches for the use of biocatalysts in production processes: non-chiral synthesis, asymmetric synthesis, and racemic and dynamic resolution. Applications for whole cells and isolated enzymes as catalysts are introduced. Finally, critical but optimistic conclusions are given.

Multilayer structures in lipid monolayer films containing surfactant protein C: effects of cholesterol and POPE.

The influence of cholesterol and POPE on lung surfactant model systems consisting of DPPC/DPPG (80:20) and DPPC/DPPG/surfactant protein C (80:20:0.4) has been investigated. Cholesterol leads to a condensation of the monolayers, whereas the isotherms of model lung surfactant films containing POPE exhibit a slight expansion combined with an increased compressibility at medium surface pressure (10-30 mN/m). An increasing amount of liquid-expanded domains can be visualized by means of fluorescence light microscopy in lung surfactant monolayers after addition of either cholesterol or POPE. At surface pressures of 50 mN/m, protrusions are formed which differ in size and shape as a function of the content of cholesterol or POPE, but only if SP-C is present. Low amounts of cholesterol (10 mol %) lead to an increasing number of protrusions, which also grow in size. This is interpreted as a stabilizing effect of cholesterol on bilayers formed underneath the monolayer. Extreme amounts of cholesterol (30 mol %), however, cause an increased monolayer rigidity, thus preventing reversible multilayer formation. In contrast, POPE, as a nonbilayer lipid thought to stabilize the edges of protrusions, leads to more narrow protrusions. The lateral extension of the protrusions is thereby more influenced than their height.

Interaction analysis of chimeric metal-binding green fluorescent protein and artificial solid-supported lipid membrane by quartz crystal microbalance and atomic force microscopy.

Non-specific adsorption and specific interaction between a chimeric green fluorescent protein (GFP) carrying metal-binding region and the immobilized zinc ions on artificial solid-supported lipid membranes was investigated using the quartz crystal microbalance technique and the atomic force microscopy (AFM). Supported lipid bilayer, composed of octanethiol and 1,2-dipalmitoyl-sn-glycero-3-phosphocholine/1,2-dioleoyl-sn-glycero-3-[N-(5-amino-1-carboxypentyl iminodiacetic acid)succinyl] (NTA-DOGS)-Zn2+, was formed on the gold electrode of quartz resonator (5 MHz). Binding of the chimeric GFP to zinc ions resulted in a rapid decrease of resonance frequency. Reversibility of the process was demonstrated via the removal of metal ions by EDTA. Nanoscale structural orientation of the chimeric GFP on the membrane was imaged by AFM. Association constant of the specific binding to metal ions was 2- to 3-fold higher than that of the non-specific adsorption, which was caused by the fluidization effect of the metal-chelating lipid molecules as well as the steric hindrance effect. This infers a possibility for a further development of biofunctionalized membrane. However, maximization is needed in order to attain closer advancement to a membrane-based sensor device.