Role of Glycerol Permeation in the Bloodstream Form of Trypanosoma brucei*

SYNOPSIS. Under aerobic conditions, we have determined glycerol uptake in the long slender (LS) bloodstream form of Trypanosoma (Trypanozoon) brucei brucei by studying glycerophosphate accumulation in the parasites. The coupled enzyme theory applies to the permeation-phosphorylation sequence. Glycerol passage through the plasma membrane is asymmetric, the efflux process being favored over the influx process. No free diffusion of glycerol can be detected even under conditions under which free glycerol accumulates within the cells; most probably, glycerol permeation is mediated by a specific transport system. In the absence of respiratory activities, glycerol is known to be an end-product of T. brucei glycolysis; its production from glycerophosphate should allow ATP synthesis. The observed efflux of free glycerol following intracellular accumulation of glycerophosphate confirms the hypothesis that glycerol production occurs through reversal of glycerol kinase activity. We conclude that in vivo the role of the carrier-mediated asymmetric permeation process is to prevent inhibition of the reversal of the glycerol kinase-mediated reaction by removing free glycerol.     

Hydrolysis of butteroil by immobilized lipase using a hollow-fiber reactor: part II. Uniresponse kinetic studies

A lipase from Aspergillus niger immobilized by adsorption on microporous, polypropylene hollow fibers was used to effect the hydrolysis of the glycerides of melted butterfat at 40 degrees C and pH 7.0. Mcllvane buffer was pumped through the lumen and melted butterfat was pumped courrently through the shell side of a shell-and-tube reactor. Nonlinear regression methods were employed to determine the kinetic parameters of three nested rate expressions derived from a Ping Pong Bi Bi enzymatic mechanism coupled with three nested rate expressions for the thermal deactivation of the enzyme. For the reaction conditions used in this research, a four-parameter rate expression (which includes a two-parameter deactivation rate expression and a two-parameter hydrolysis rate expression) is sufficient to model the overall release of free fatty acids from the triglycerides of butterfat as a function of space time and time elapsed after immobilization. At a space time of 3.7 h immediately after immobilization of lipase, 50% of the fatty acid residues esterified in the sn-1,3 positions of the triglycerides can be released in the hollow-fiber reactor.     

The Influence of Fatty Acid and Glycerol on the Kinetics of Fat Hydrolysis by Candida Rugosa Lipase in a Membrane Reactor

The kinetics of lipid-hydrolysis by Candida rugosa lipase was investigated in a membrane reactor and in an emulsion system. Two models were chosen to describe the kinetics of the enzyme:

(1) The hydrolysis of triglycerides to fatty acids was considered to be a chain reaction with the intermediary products di- and mono-glyceride; each step was assumed to be a reversible second-order reaction. The reaction rate constants were determined from batch experiments. The experimental results could be described with this model.

(2) For process optimization and control, a model based on the power law was developed. For this model, the rate of hydrolysis was measured as a function of fatty acid and glycerol concentrations. Relations for the initial rate and equilibrium ester fraction as a function of the glycerol concentration were determined. Further, the reaction rate could be described with the power-law model with a power of 1.75 in the hydrolyzable ester fraction for a wide range of glycerol concentrations. The model with power 1.75 gave much better results when compared to a similar first order model. Although simpler, the first order model can not be used. The power law model was applied in the simulation of a reactor composed of three modules. The fatty acid production rate was calculated for this reactor system as a function of the outgoing glycerol concentration at different conditions.     

Biodiesel synthesis in a solvent-free system by recombinant Rhizopus oryzae: comparative study between a stirred tank and a packed-bed batch reactor

A simultaneous synthesis of biodiesel, as fatty acid methyl esters, and monoacylglycerols catalysed by the recombinant Rhizopus oryzae lipase immobilized by adsorption on Relizyme OD/403M is presented. The use of this 1(3)-positional specific lipase prevents the formation of glycerol as a by-product, thus avoiding its drawbacks. The synthesis was carried out in a solvent-free system and it has been studied in two different reactor systems: stirred tank and packed-bed reactor. Stirred tank reactor presented a high-initial reaction rate and achieved a 33.6% yield, which corresponds to a value of 50.4% of the maximum yield that can be achieved with a 1(3)-positional specific lipase. In packed-bed reactor there was a smaller initial reaction rate, but it was achieved a 49.1% yield, which corresponds to a 73.6% of the maximum yield. When a second batch is performed, the yield decreased only 4% when packed-bed reactor is employed whereas a drastic decrease is observed in a stirred tank operation. Therefore, packed-bed reactor showed a best performance and minor damage to the biocatalyst.     

Hydrolysis of butteroil by immobilized lipase using a hollow-fiber reactor: IV. Effects of temperature

A lipase from Aspergillus niger, immobilized by adsorption on microporous polypropylene hollow fibers, was used to effect the hydrolysis of the glycerides of melted butterfat at pH. 7.0 at 40, 50, 55, and 60 degrees C. Mcllvane buffer was pumped upward through the lumen, and melted butterfat was pumped upward through the shell side of a hollow fiber reactor. Nonlinear regression methods were employed to determine the kinetic parameters of models based on combinations of three nested rate expressions for the hydrolysis reaction with three nested rate expressions for thermal deactivation of the enzyme. A rate expression containing four lumped parameters is sufficient to model the release of free fatty acids as a function of reactor space time and time elapsed after immobilization. Nonlinear regression methods were also employed in global fits of the data to rate expressions containing an explicit dependence on temperature. For the reaction conditions used in this research, a 14-parameter rate expression is necessary to accurately model the overall release of free fatty acids as a continuous function of the absolute temperature, initial substrate concentrations, reactor space time, and time elapsed after immobilization of the lipase.     

Process engineering and optimization of glycerol separation in a packed-bed reactor for enzymatic biodiesel production

A process model for efficient glycerol separation during methanolysis in an enzymatic packed-bed reactor (PBR) was developed. A theoretical glycerol removal efficiency from the reaction mixture containing over 30% methyl esters was achieved at a high flow rate of 540 ml/h. To facilitate a stable operation of the PBR system, a batch reaction prior to continuous methanolysis was conducted using oils with different acid values and immobilized lipases pretreated with methyl esters. The reaction system successfully attained the methyl ester content of over 30% along with reduced viscosity and water content. Furthermore, to obtain a high methyl ester content above 96% continuously, long-term lipase stability was confirmed by operating a bench-scale PBR system for 550 h, in which the intermediates containing methyl esters and residual glycerides were fed into the enzyme-packed columns connected in series. Therefore, the developed process model is considered useful for industrial biodiesel production.     

Efficient preparation of (R)-alpha-monobenzoyl glycerol by lipase catalyzed asymmetric esterification: optimization and operation in packed bed reactor

Optically active (R)-alpha-monobenzoyl glycerol (MBG) was synthesized by Candida antarctica lipase B (CHIRAZYME L-2) catalyzed asymmetric esterification of glycerol with benzoic anhydride in organic solvents. Various conditions, such as the type and composition of the organic solvent, water content of the system, reaction temperature, and concentrations of the substrates were systematically examined and optimized in screw-capped test tubes with respect to both the reaction rate and the enzyme selectivity. 1,4-Dioxane was found to be the best solvent and no additional water was needed for the system. The optimum temperature was around 30 degrees C, while the most suitable substrate concentrations were 100 mM each for glycerol and benzoic anhydride, respectively. However, when excessive anhydride (e.g., 200 mM) was used, the produced MBG could be further transformed into 1,3-dibenzoyl glycerol (DBG) by the same enzyme with a priority to (S)-MBG, resulting in a significant improvement of the product optical purity from ca. 50-70% e.e. Under optimal conditions (100 mM glycerol, 100-200 mM benzoic anhydride, dioxane, 25-30 degrees C), the enzymatic synthesis of (R)-MBG was successfully operated in a packed-bed reactor for about 1 week, with an average productivity of 0.79 g MBG/day/g biocatalyst in the case of continuous operation and 0.94 g MBG/day/g biocatalyst in the case of semicontinuous operation. After refinement and preferential crystallization of the crude product, (R)-MBG could be obtained in an almost optically pure form (>98% e.e.).     

Reactor optimization for alpha-1,2 glucooligosaccharide synthesis by immobilized dextransucrase

The immobilization of dextransucrase in Ca-alginate beads relies on the close association between dextran polymer and dextransucrase. However, high amounts of dextran in the enzyme preparation drastically limit the specific activity of the immobilized enzyme (4 U/mL of alginate beads). Moreover, even in the absence of diffusion limitation at the batch conditions used, the enzyme behavior is modified by entrapment so that the dextran yield increases and the alpha-1,2 glucooligosaccharides (GOS) are produced with a lower yield (46.6% instead of 56.7%) and have a lower mean degree of polymerization than with the free dextransucrase. When the immobilized catalyst is used in a continuous reaction, the reactor flow rate necessary to obtain high conversion of the substrates is very low, leading to external diffusion resistance. As a result, dextran synthesis is even higher than in the batch reaction, and its accumulation within the alginate beads limits the operational stability of the catalyst and decreases glucooligosaccharide yield and productivity. This effect can be limited by using reactor columns with length to diameter ratio > or =20, and by optimizing the substrate concentrations in the feed solution: the best productivity obtained was 3.74 g. U(-1). h(-1), with an alpha-1,2 GOS yield of 36%.     

Subcellular distribution and kinetic properties of soluble and particulate-associated bovine adrenal 21vcerol kinase

Summary The subcellular distribution and substrate kinetics of soluble and particulate-associated bovine adrenal glycerol kinase have been investigated. Whole adrenal, adrenal cortex and adrenal medulla were examined for distribution of glycerol kinase between soluble and particulate fractions. No major differences in distribution were noted between these tissues; of the total homogenate activity, 0–20% sedimented with the nuclear fraction, 24–36% sedimented with the post-nuclear fraction and 62–69% remained soluble. Steadystate kinetic parameters of glycerol kinase activity were compared in the soluble and mitochondrial fractions. The K_m for glycerol in the soluble fraction was 6.3 ± 0.1 M and in the mitochondrial fraction was 4.0 = 0.3 M. The K_m for ATP in soluble fraction was 12.8 1.5 and in the mitochondrial fraction was 5.3 ± 1.6. Release of adrenal glycerol kinase from the mitochondria) fraction was investigated using inorganic phosphate, ATP and glycerol 3-phosphate. Of these compounds, only ATP and glycerol 3-phosphate were effective in releasing particulate-associated glycerol kinase. Inorganic phosphate had no effect upon release. Particulate-associated glycerol kinase activity of the mitochondrial fraction was stimulated by addition of succinate and ADP and was inhibited by addition of atractyloside. The data presented here indicate that bound glycerol kinase found within the mitochondrial fraction is kinetically distinct from soluble glycerol kinase and binding to mitochondria is responsive to substrate and product levels within the physiological range.     

Human and rat adrenal glycerol kinase: subcellular distribution and bisubstrate kinetics

Summary The subcellular distribution of adrenal glycerol kinase in man and rat are reported and the bisubstrate kinetics of the soluble enzyme are compared in these two species. The specific activity of glycerol kinase in human whole adrenal homogenate (145 µU/mg protein) was 3 times that found in rat whole adrenal homogenate (48 µU/mg protein). In both species 8% of the total glycerol kinase activity was associated with the nuclear pellet fraction. In human, 62% of the total activity was soluble, while 24% was associated with the postnuclear particulate fraction. Rat glycerol kinase activity was also predominantly soluble: 69% of the total activity was soluble and 13% was in the postnuclear particulate fraction. The apparent K_m for glycerol in soluble adrenal glycerol kinase was similar in both species, 2.8 µM in human and 3.1 µM in rat. The apparent K_m for ATP in soluble human adrenal glycerol kinase was 22.0 µM. In rat the enzyme did not appear to follow Michaelis-Menten kinetics with ATP as substrate. The V_max for the soluble enzyme was similar in both human and rat.This report provides a background to biochemical investigations on human glycerol kinase deficiency, an inborn error of metabolism which may be characterized by adrenal hypoplasia and insufficiency.     

Use of stable emulsion to improve stability, activity, and enantioselectivity of lipase immobilized in a membrane reactor

The enantiocatalytic performance of immobilized lipase in an emulsion membrane reactor using stable emulsion prepared by membrane emulsification technology was studied. The production of optical pure (S)-naproxen from racemic naproxen methyl ester was used as a model reaction system. The O/W emulsion, containing the substrate in the organic phase, was fed to the enzyme membrane reactor from shell-to-lumen. The enzyme was immobilized in the sponge layer (shell side) of capillary polyamide membrane with 50 kDa cut-off. The aqueous phase was able to permeate through the membrane while the microemulsion was retained by the thin selective layer. Therefore, the substrate was kept in the enzyme-loaded membrane while the water-soluble product was continuously removed from the reaction site. The results show that lipase maintained stable activity during the entire operation time (more than 250 h), showing an enantiomeric excess (96 +/- 2%) comparable to the free enzyme (98 +/- 1%) and much higher compared to similar lipase-loaded membrane reactors used in two-separate phase systems (90%). The results demonstrate that immobilized enzymes can achieve high stability as well as high catalytic activity and enantioselectivity.     

Development of a Polyaniline-coated Monolith Reactor for the Synthesis of Cephalexin Using Penicillin G Acylase Aggregates

A monolith reactor for the synthesis of cephalexin was developed using capillary columns. The micro channel in the monolith reactor was coated with polyaniline (PANI), and penicillin G acylase was aggregated with PANI using 0.5% of glutaraldehyde as a cross-linker. The developed monolith reactor exhibited many advantages over other enzyme reactors such as batch and continuous reactors. It showed fast enzyme reaction rates owing to the decrease in external mass transfer and internal diffusion limitations. The reactor can easily be scaled up by bundling together multiple monolith reactors, enabling a corresponding increase in feed rate. Furthermore, the monolith reactor showed good operational stability, with 95% of its original activity maintained after 48 h of continuous operation. The PANI coating on the surface of the capillary column increased the enzyme immobilization capacity and conversion was increased from 15.4% to 70.6% after PANI coating. The conversion ratio increased to approximately 70.6% with an increase in residence time and reactor length.     

Theoretical analysis of G6P production and simultaneous ATP regeneration by conjugated enzymes in an ultrafiltration hollow-fiber reactor

The performance of an ultrafiltration hollow-fiber reactor, in which the enzymatic synthesis of glucose 6-phosphate from glucose and cofactor ATP and the enzymatic regeneration of ATP from ADP and acetyl phosphate are performed simultaneously, was analyzed theoretically. A simple analytical model in which the liquid flowing in the fiber tubes is assumed to be plug flow, and the radial concentration gradients in the tube and shell sides are both neglected, could simulate the reactor performance with satisfactory accuracy. The simulation elucidated the effects of the reactor configurations and various operational conditions on glucose conversion, ATP recycle number, and space-time yield. If the fiber tubes, through which the permeability of the relevant components such as substrates is high, were packed as much as possible in the reactor, good reactor performance could be expected. Furthermore, with a sufficiently high enzyme concentration, low ATP concentration in the feed solution, and appropriate space velocity, good space-time yield with high glucose conversion and with very high ATP recycle number is theoretically possible.     

Repeated batch and continuous operations for phosphatidylglycerol synthesis from phosphatidylcholine with immobilized phospholipase D

Summary The repeated batch and continuous operations for transphosphatidylation reaction were carried out for phosphatidylglycerol (PG) synthesis from phosphatidylcholine (PC) with the help of immobilized cabbage phospholipase D (PLD) in the presence of glycerol. The biphasic reaction system was used which included the aqueous phase containing immobilized PLD along with high concentrations of glycerol (30%–50%) and buffer, whereas the main part of substrate (PC) and products (mainly PG) formed were in the organic phase (diethyl ether).Octyl-Sepharose CL-4B having a hydrophobic octyl group was chosen for the PLD immobilization. Both immobilization yield and activity yield of immobilized enzyme were 100%. The effects of solvents, temperature and glycerol concentrations on the immobilized PLD were examined. Repeated batch conversion of PC (15 g/l) to PG was examined with the immobilized PLD in 30% glycerol. In all five batch cycles examined, 100% selectivity was obtained and there was no significant decrease in the fractional conversion of PC to PG (98%–99%) in the first three batch cycles. In the cases of a packed-bed reactor (PBR) and a continuous stirred-tank reactor (CSTR) used for continuous synthesis of PG with the immobilized PLD, the operational stabilities of the immobilized enzyme were almost the same (half life=14 h at 30°C) when purified PC was used, while in the case of partially purified PC in CSTR the half life increased more than five times.Abbreviations used PC phosphatidylcholine - PG phosphatidylglycerol - PA phosphatidic acid - PLD phospholipase D - PBR packed bed reactor - CSTR continuous stirred tank reactor Studies on enzymatic conversion of phospholipids (III)     

Characterization of a whole‐cell catalyst co‐expressing glycerol dehydrogenase and glucose dehydrogenase and its application in the synthesis of L‐glyceraldehyde

A whole‐cell catalyst using Escherichia coli BL21(DE3) as a host, co‐expressing glycerol dehydrogenase (GlyDH) from Gluconobacter oxydans and glucose dehydrogenase (GDH) from Bacillus subtilis for cofactor regeneration, has been successfully constructed and used for the reduction of aliphatic aldehydes, such as hexanal or glyceraldehyde to the corresponding alcohols. This catalyst was characterized in terms of growth conditions, temperature and pH dependency, and regarding the influence of external cofactor and permeabilization. In the case of external cofactor addition we found a 4.6‐fold increase in reaction rate caused by the addition of 1 mM NADP⁺. Due to the fact that pH and temperature are also factors which may affect the reaction rate, their effect on the whole‐cell catalyst was studied as well. Comparative studies between the whole‐cell catalyst and the cell‐free system were investigated. Furthermore, the successful application of the whole‐cell catalyst in repetitive batch conversions could be demonstrated in the present study. Since the GlyDH was recently characterized and successfully applied in the kinetic resolution of racemic glyceraldehyde, we were now able to transfer and establish the process to a whole‐cell system, which facilitated the access to L ‐glyceraldehyde in high enantioselectivity at 54% conversion. All in all, the whole‐cell catalyst shows several advantages over the cell‐free system like a higher thermal, a similar operational stability and the ability to recycle the catalyst without any loss‐of‐activity. The results obtained making the described whole‐cell catalyst an improved catalyst for a more efficient production of enantiopure L ‐glyceraldehyde. Biotechnol. Bioeng. 2010;106: 541–552. © 2010 Wiley Periodicals, Inc.     

Continuous ATP production by spinach thylakoid in a stirred tank reactor

Spinach thylakoid was immobilized by two different methods for the purpose of retention within a continuous-flow stirred tank reactor (CSTR). The glutaraldehyde crosslinked albumin polymer method completely inactivated the cyclic ATP photophosphorylation of thylakoid. In contrast, agarose-entrapped thylakoid retained about 17% of the activity of the cyclic photophosphorylation of non-immobilized thylakoid. This activity declined continuously during ATP production in the CSTR. Fifty percent of the initial activity was lost within about 5.5 h. Ascorbate was found to increase the stability of ATP photophosphorylation; about twice as much ATP was produced at the optimal ascorbate concentration of 5 mM. Under the optimal dilution rate of 2.36 h⁻¹, about 60 μmol of ATP per mg chlorophyll were produced in 20 h by agarose-entrapped thylakoid in the CSTR. These results showed that, compared to non-immobilized thylakoid in batch operation, agarose-entrapped thylakoid produced only a low amount of ATP under continuous operation.     

Biodiesel production using Aspergillus niger as a whole‐cell biocatalyst in a packed‐bed reactor

Enzymatic lipase transesterification of palm oil to biodiesel in a packed‐bed reactor (PBR) using a novel strain of the fungus Aspergillus niger, immobilized within polyurethane biomass support particles (BSPs), was investigated. A three‐step addition of methanol was used to reduce lipase inhibition by immiscible methanol. The influence of water content and PBR flow rate was investigated. FAME yield was enhanced with an increase of PBR flow rate in the range of 0.15–30 L h^?1, where inefficient mixing of the reaction mixture at lower flow rates resulted in low conversion rates i.e. 69% after 72‐h reaction. Adding the third mole equivalent of methanol resulted in lipase inhibition due to methanol migration into the accumulated glycerol layer. Glutaraldehyde (GA) solution (0.5 vol.%) was used to stabilize lipase activity, which led to a high FAME yield (>90%) in the PBR after 72‐h of reaction time at a flow rate of 15 L h^?1, and a water content of 15%. Moreover, a high conversion rate (>85%) was maintained after four palm oil batch conversion cycles in the PBR. In contrast, lipase activity of non‐GA‐treated cells decreased with each PBR batch cycle, where only 70% FAME was produced after the forth PBR cycle. Transesterification of palm oil in a PBR system using BSPs‐immobilized A. niger as a whole‐cell biocatalyst is a viable process for enzymatic biodiesel production.     

Immobilized glucoamylase on porous glass

A study was made to determine the controlling mass transfer resistance in the overall reaction rate for conversion of maltose to glucose, catalyzed by glucoamylase immobilized onto porous glass. For normal operation of a packed column and air-stirred batch reactor, the rate controlling step was found to be the internal resistance of simultaneous pore diffusion and chemical reaction. Experimental effectiveness factors were determined and are compared with those derived from a theoretical diffusion model based on Michaelis-Menten kinetics. Also given are temperature and pH relationships for the free and immobilized glucoamylase.     

Performance of a cutinase membrane reactor for the production of biodiesel in organic media

The enzymatic transesterification of oils with an alcohol, using recombinant cutinase of Fusarium solani pisi microencapsulated in sodium bis(2-ethylhexyl) sulfosuccinate (AOT)/isooctane reversed micelles, was performed in a membrane bioreactor (MBR). A tubular ceramic membrane with a nominal molecular weight cut off of 15,000 Da was used to retain the enzyme, and characterized in terms of rejection coefficients of the reaction components by transmission experiments. The performance of the MBR in a total recirculation-batch mode was compared with results obtained in a stirred batch tank reactor. The continuous operation of the MBR was also evaluated and the influence of the alcohol type and permeate flow rate on conversion degree and productivity (up to 500 g(product) /day/g(enzyme) was attained) were analyzed. Cutinase wild type and mutant T179C were tested for this process and the high long-term operational stability of the cutinase mutant demonstrated its potential as biocatalyst for the enzymatic continuous production of biodiesel.     

Bioreaction Engineering Leading to Efficient Synthesis of L‐Glyceraldehyd‐3‐Phosphate

Enantiopure L‐glyceraldehyde‐3‐phosphate (L‐GAP) is a useful building block in natural biological and synthetic processes. A biocatalytic process using glycerol kinase from Cellulomonas sp. (EC 2.7.1.30) catalyzed phosphorylation of L‐glyceraldehyde (L‐GA) by ATP is used for the synthesis of L‐GAP. L‐GAP has a half‐life of 6.86 h under reaction conditions. The activity of this enzyme depends on the Mg²⁺ to ATP molar ratio showing maximum activity at the optimum molar ratio of 0.7. A kinetic model is developed and validated showing a 2D correlation of 99.9% between experimental and numerical data matrices. The enzyme exhibits inhibition by ADP, AMP, methylglyoxal and Ca²⁺, but not by L‐GAP and inorganic orthophosphate. Moreover, equal amount of Ca²⁺ exerts a different degree of inhibition relative to the activity without the addition of Ca²⁺ depending on the Mg²⁺ to ATP molar ratio. If the Mg²⁺ to ATP molar ratio is set to be at the optimum value or less, inorganic hexametaphosphate (PPi6) suppresses the enzyme activity; otherwise PPi6 enhances the enzyme activity. Based on reaction engineering parameters such as conversion, selectivity and specific productivity, evaluation of different reactor types reveals that batchwise operation via stirred‐tank reactor is the most efficient process for the synthesis of L‐GAP.