Strategies for the design and operation of enzymatic reactors for the degradation of highly and poorly soluble recalcitrant compounds

The presence of recalcitrant compounds in both wastewaters and soils is an important environmental problem. Oxidative enzymes from white-rot fungi have been successfully utilised for the in vitro degradation of xenobiotics, such as the azo dye Orange II and the polycyclic aromatic hydrocarbon anthracene (compounds with high and low solubilities, respectively). Two different reactor configurations are proposed: (i) an enzymatic membrane reactor for the treatment of soluble compounds, consisting of a continuous stirred tank reactor coupled to an ultrafiltration membrane to facilitate the retention and recycling of enzyme; and (ii) a two-phase enzymatic reactor for the degradation of poorly soluble compounds, consisting of an immiscible solvent, which contains the contaminant at high concentrations, and the aqueous phase containing the enzyme and cofactors involved in the catalytic cycle. In this paper, factors affecting the design and operation of both systems are discussed, and experimental results concerning the efficiency and stability of the processes are presented.     

Economic comparison of enzymatic reactors and advanced oxidation processes applied to the degradation of phenol as a model compound

Abstract

Some micropollutants present in wastewaters are barely removed in sewage treatment plants. In many cases a post-treatment process based on separation and/or oxidation has to be applied. The aim of this study was the technical and economic comparison of enzymatic technologies with other advanced oxidation processes (AOPs) for the degradation of phenol. Batch and continuous enzymatic reactors, using free and immobilized manganese peroxidase (MnP, EC 1.11.1.13), were considered. Continuous degradation of phenol in an enzymatic membrane reactor was shown to be the fastest process and degradation in a continuous reactor with immobilized enzyme involved the lowest consumption of enzyme. However, the immobilization process increased the enzyme cost 100-fold. A continuous enzymatic membrane reactor gave high degradation efficiency and may be a viable technology for phenol removal when compared with other AOPs from both technical and economic points of view.     

Enzymatic degradation of low soluble compounds in monophasic water: solvent reactors. Kinetics and modeling of anthracene degradation by MnP

Polycyclic aromatic hydrocarbons (PAHs) are toxic compounds presenting low water solubility and high hydrophobicity, which greatly hampers their natural biodegradation. The enzymatic degradation of a model compound, anthracene, was evaluated in presence of a miscible solvent for an increased solubility. Manganese peroxidase, a ligninolytic enzyme from white-rot fungi, was used as biocatalyst in a medium containing acetone. The kinetic parameters of the enzymatic degradation of anthracene, obtained from fed-batch experiments, were applied to model the operation of a continuous reactor. Kinetics comprised a Michaelis-Menten equation, modified with an autocatalytic term, assumed to the effect of quinones acting as electron carriers, and a logistic function related to enzyme activity. The continuous reactor has been operated for 108 h, attaining a 90% of anthracene degradation, which demonstrated the feasibility of the system for its application in the removal of poorly soluble compounds. The model of this reactor permitted to predict accurately anthracene degradation in different conditions, such as external addition of anthraquinone and different enzymatic activities.     

Sequential reactors for the removal of endocrine disrupting chemicals by laccase immobilized onto fumed silica microparticles

Abstract

The main objective of this study is the evaluation of the capability of laccase from Myceliophthora thermophila immobilized on fumed silica microparticles (fsMP) for the removal of endocrine disrupting chemicals (EDCs) in two enzymatic reactor configurations. This type of support can also be magnetized to allow the straightforward separation of the biocatalyst under a magnetic field. The support exhibited excellent biocompatibility with the enzyme, superior tolerance to pH and temperature as well as improved stability in comparison with the free enzyme, even in the presence of organic solvents and enzyme inhibitors. The technical feasibility of the removal of EDCs by immobilized laccase was assessed in two types of enzymatic reactors operated in sequential mode: a membrane reactor using fsMP-laccase and a reactor with magnetic separation using magnetized fsMP-laccase. The extent of transformation for the target compounds: bisphenol A (BPA) and 17β-estradiol (E2) was high and comparable to free laccase in both systems (up to 80%). The possibility of reusing the immobilized enzyme, especially for magnetized supports, offers an interesting approach in the development of enzyme based processes for the biotransformation of emerging pollutants.     

Dynamic modeling of an enzymatic membrane reactor for the treatment of xenobiotic compounds

A membrane enzymatic reactor, consisting of a stirred tank coupled to an ultrafiltration membrane was set up for the enzymatic oxidation of xenobiotic compounds. The azo dye Orange II was selected for the model compound and manganese peroxidase for the oxidative enzyme. The ligninolytic cycle was initiated and maintained by the controlled addition of all factors (reactants, mediators, and stabilizers) at suitable rates. Considering the distinctiveness of this process, in which the substrate to be oxidized is not the primary substrate for the enzyme, a kinetic model was developed. The azo dye concentration and hydrogen peroxide addition rate were found to be the main factors affecting the process. The reaction kinetics was defined using a Michaelis-Menten model with respect to the Orange II concentration and a first-order linear dependence relative to the H(2)O(2) addition rate. The dynamic model, which takes into account both the kinetics and the hydraulics of the system, was validated by comparing the experimental results in continuous operation under steady and non-steady state to model predictions. In particular, the model predicted the behavior of the system when unexpected alterations in steady-state operation occurred. Furthermore, the model allowed us to obtain the most appropriate H(2)O(2)/Orange II ratio in the feed to maximize the process efficiency.     

Dye decolorization by manganese peroxidase in an enzymatic membrane bioreactor

In the present work an enzymatic membrane reactor (EMR) for the oxidation of azo dyes by manganese peroxidase (MnP) has been developed. The configuration consisted of a stirred tank reactor coupled with an ultrafiltration membrane. The membrane allowed for most of the enzymatic activity to be recovered while both the parent dye and the degradation products could pass through. Different operational strategies (batch, fed-batch, and continuous) and parameters such as enzyme activity, H(2)O(2) feeding rate, hydraulic retention time (in continuous operation), and dye loading rate were studied. At best conditions, a continuous operation with a dye decolorization higher than 85% and minimal enzymatic deactivation was feasible for 18 days, attaining an efficiency of 42.5 mg Orange II oxidized/MnP unit consumed.     

A novel reactor concept for the enzymatic reduction of poorly soluble ketones

Reductions of poorly soluble ketones often suffer from low total turnover numbers conferring to the coenzyme and large volumes which are needed for the conversion. The novel emulsion membrane reactor overcomes these limitations. From an emulsion consisting of an organic substrate and an aqueous buffer phase, the aqueous phase is separated selectively by using a hydrophilic ultrafiltration membrane and fed to a subsequent enzyme membrane reactor. The product outflow is recirculated to the emulsion stirred vessel and, due to the partition coefficients, the aqueous phase is recharged with substrate while the product is extracted. This new reactor concept will be compared to the classical enzyme membrane reactor. The latter was operated under the same conditions over a period of 4 months at a space-time yield of 21.2 g l⁻¹ day⁻¹. As a model system the enantioselective reduction of 2-octanone to (S)-2-octanol (ee > 99.5%) is used, carried out by a carbonyl reductase from Candida parapsilosis. NADH is regenerated by formate dehydrogenase from Candida boidinii. In comparison to the classical enzyme membrane reactor the total turnover number could be increased by a factor 9 using the novel emulsion membrane reactor.     

Improved operational stability of cell-free glucose-fructose oxidoreductase from Zymomonas mobilis for the efficient synthesis of sorbitol and gluconic acid in a continuous ultrafiltration membrane reactor

For the continuous, enzymatic synthesis of sorbitol and gluconic acid by cell-free glucose-fructose oxidoreductase (GFOR) from Zymomonas mobilis, the principal determinants of productivity have been identified. Most important, the rapid inactivation of the soluble enzyme during substrate conversion can be avoided almost completely when weak bases such as tris(hydroxymethyl)aminomethan or imidazol are used for the titration of the produced gluconic acid and when 5-10 mM dithiothreitol are added to prevent thiol oxidations. With regard to a long-term operational stability of the enzyme for continuous syntheses, thermal deactivation becomes significant at reaction temperatures above 30 degrees C. Without any additional purification being required, the crude cell extract of Z. mobilis can be employed in a continuous ultrafiltration membrane reactor over a time period of more than 250 h without significant decrease in substrate conversion or enzyme activity. The use of soluble GFOR thus appears to be an interesting alternative to employing permeabilized cells of Zymomonas for the production of sorbitol and gluconic acid and may be superior with regard to reactor productivities, at comparable operational stabilities.     

A chemiluminescence automatic analyser for the measurement of biological compounds

A compact automated analyser which could analyse constituents in biological fluids with a small sample volume and in a short time has been developed. The instrument was composed of a flow injection analysis system equipped with chemiluminometric detection and an immobilized enzyme column reactor used in combination. Chemiluminescence has high sensitivity, and its reaction proceeds very quickly. Furthermore, an immobilized enzyme column reactor can produce a sufficient amount of hydrogen peroxide from compounds in serum in a short time. When enzymes are used as reagents for the analysis of substances in blood or blood serum, the final signals emitted by different enzyme reactions are usually not only hydrogen peroxide but also ammonia, NAD(P)H and so on. However, the practical chemiluminescence method for ammonia and NAD(P)H has not been established. We have discovered a new practical method for ammonia and NAD(P)H using an enzyme column reactor consisting of both immobilized L -glutamate dehydrogenase and L -glutamate oxidase. The determinations of glucose and uric acid in serum by chemiluminometry after production of hydrogen peroxide by the respective oxidases are presented. A newly chemiluminometric determination of ammonia, NAD(P)H and its applications to other enzymatic analyses that give ammonia and NAD(P)H as a final signal are also described.     

Glucose oxidation in a dual hollow fiber bioreactor with a silicone tube oxygenator

A dual hollow fiber bioreactor, consisting of an outer silicone membrane for oxygen supply and an inner polyamide membrane for substrate permeation, was used as an immobilized enzyme reactor to carry out enzymatic glucose oxidation. Attaching a silicone tube oxygenator to provide an additional oxygen supply improved the conversion in glucose oxidation when the oxygen supply was rate-limiting. The reactor was operated in both diffusion and ultrafiltration modes. In the latter case, the conversion was much higher, but the stability of the immobilized enzyme was better maintained in the diffusion mode. As the inlet glucose concentration increased from 10mM to 500mM, the conversion decreased from 70 to 20%.     

Insulin and glucagon degradation by the kidney. II. Characterization of the mechanisms at neutral pH.

Examination of insulin and glucagon degradation by rat kidney subcellular fractions revealed that most degrading activity was localized to the 100 000 X g pellet and 100 000 X g supernatant fractions. Further characterization of the degrading activities of the 100 000 X g pellet and supernatant suggested that three types of enzymatic activity were present at neutral pH. From the cytosol an enzyme with characteristics of the insulin glucagon protease of skeletal muscle was purified. This enzyme appeared to be responsible for insulin degradation by the kidney at physiological insulin concentrations. This enzyme also contributed to glucagon degradation but was not the most active mechanism for this. In the 100 000 X g pellet at least two separate enzymatic activities were present. One of these had properties consistent with those described for glutathione insulin transhydrogenase and appeared to be responsible for insulin degradation at high insulin concentration. The other enzyme was associated with the brush border and had properties consistent with the brush border neutral protease. This enzyme appeared responsible for glucagon degradation at both low and high substrate concentrations. An apparent marked synergism between the 100 000 X g pellet and the 100 000 X g supernatant was noted for insulin degradation at physiological insulin concentrations. Pellet glucagon-degrading activity and soluble insulin-degrading activity were necessary for this. The mechanism was found to be limited insulin degradation by the soluble enzyme resulting in both trichloroacetic acid-precipitable trichloroacetic acid-soluble fragments followed by further degradtion of the fragments by the glucagon-degrading enzyme resulting in an additional increase in trichloroacetic acid-soluble products.     

Pseudomonas stutzeri soluble nitrate reductase alphabeta-subunit is a soluble enzyme with a similar electronic structure at the active site as the inner membrane-bound alphabetagamma holoenzyme

A two-subunit (alphabeta) form of dissimilatory nitrate reductase from Pseudomonas stutzeri strain ZoBell was separated from the membrane-residing gamma-subunit by a heat solubilization step. Here we present an optimized purification protocol leading to a soluble alphabeta form with high specific activity (70 U/mg). The soluble form has the stoichiometry alpha(1)beta(1) consisting of the 130 kDa alpha-subunit and the 58 kDa beta-subunit. We did not observe any proteolytic cleavage in the course of the heat solubilization. The enzyme is competively inhibited by azide, but not by chlorate. It exhibits a K(M) value of 3.2 mM for nitrate. We compare the enzymatic and electron paramagnetic resonance (EPR) spectroscopic properties of the alphabeta form with the alphabetagamma holoenzyme which resides in the membrane and can be prepared by detergent extraction. The nearly identical EPR spectra for the Mo(V) signal of both enzyme preparations show that the active site is unaffected by the heat step. The factors influencing the binding of the alpha- and beta-subunit to the gamma-subunit are discussed.     

Continuous removal of endocrine disruptors by versatile peroxidase using a two‐stage system

The oxidant Mn³⁺‐malonate, generated by the ligninolytic enzyme versatile peroxidase in a two‐stage system, was used for the continuous removal of endocrine disrupting compounds (EDCs) from synthetic and real wastewaters. One plasticizer (bisphenol‐A), one bactericide (triclosan) and three estrogenic compounds (estrone, 17β‐estradiol, and 17α‐ethinylestradiol) were removed from wastewater at degradation rates in the range of 28–58 µg/L·min, with low enzyme inactivation. First, the optimization of three main parameters affecting the generation of Mn³⁺‐malonate (hydraulic retention time as well as Na‐malonate and H₂O₂ feeding rates) was conducted following a response surface methodology (RSM). Under optimal conditions, the degradation of the EDCs was proven at high (1.3–8.8 mg/L) and environmental (1.2–6.1 µg/L) concentrations. Finally, when the two‐stage system was compared with a conventional enzymatic membrane reactor (EMR) using the same enzyme, a 14‐fold increase of the removal efficiency was observed. At the same time, operational problems found during EDCs removal in the EMR system (e.g., clogging of the membrane and enzyme inactivation) were avoided by physically separating the stages of complex formation and pollutant oxidation, allowing the system to be operated for a longer period (～8 h). This study demonstrates the feasibility of the two‐stage enzymatic system for removing EDCs both at high and environmental concentrations. © 2015 American Institute of Chemical Engineers Biotechnol. Prog., 31:908–916, 2015     

Production of dextransucrase by Leuconostoc mesenteroides immobilized in calcium-alginate beads: I. Batch and fed-batch fermentations

In batch fermentation Leuconostoc mesenteroides immobilized in calcium alginate beads produced a total dextransucrase activity equal to about 93% of that by free, suspended bacterial cells under comparable conditions in a bubble column reactor. Continuous sucrose feeding (5 g/L h) to the immobilized-cell culture in the airlift bioreactor increased production of enzymatic activity by about 107% compared with ordinary batch operation of this reactor. About 14% of the enzymatic activity produced by the immobilized cells appears as soluble activity in the cell-free broth compared with about 40% in case of free cells. In an airlift bioreactor, both the soluble and the intact (sorbed and entrapped) enzymatic activity produced by the immobilized bacterial cells was about 34% greater under automatic pH control, compared to that produced in a bubble column reactor with only manual pH control. During formation of dextran by intact enzyme within cells and beads, declines are observed in apparent enzymatic activity.     

Biocatalytic generation of Mn(III)-chelate as a chemical oxidant of different environmental contaminants

The objective of this study was to investigate the enzymatic generation of the Mn(3+) -malonate complex and its application to the process of oxidizing several organic compounds. The experimental set-up consisted of an enzymatic reactor coupled to an ultrafiltration membrane, providing continuous generation of Mn(3+) -malonate from a reaction medium containing versatile peroxidase (an enzyme produced by Bjerkandera adusta strain BOS55), H(2) O(2) , MnSO(4,) and malonate. The effluent of the enzymatic reactor was introduced into a batch-stirred reactor to oxidize three different classes of compounds: an azo dye (Orange II), three natural and synthetic estrogens, and a polycyclic aromatic hydrocarbon (anthracene). The enzymatic reactor provided the Mn(3+) complex under steady-state conditions, and this oxidative species was able to transform the three classes of xenobiotics considerably (90-99%) with negligible loss of activity.     

Comparison of the Soluble and Membrane-Bound Forms of the Puromycin-Sensitive Enkephalin-Degrading Aminopeptidases from Rat

Enkephalin degradation in brain has been shown to be catalyzed, in part, by a membrane-bound puromycin-sensitive aminopeptidase. A cytosolic puromycin-sensitive aminopeptidase with similar properties also has been described. The relationship between the soluble and membrane forms of the rat brain enzyme is investigated here. Both of these aminopeptidase forms were purified from rat brain and an antiserum was generated to the soluble enzyme. Each of the aminopeptidases is composed of a single polypeptide of molecular mass 100 kilodaltons as determined by sodium dodecyl sulfate-polyacrylamide gel electrophoresis and size-exclusion chromatography. The antisoluble aminopeptidase antiserum reacts with both enzyme forms on immunoblots and inhibits both with nearly identical inhibition curves. The isoelectric points (pI = 5.0) of both forms were shown to be identical. N-terminal sequencing yielded a common sequence (P-E-K-R-P-F-E-R-L-P-T-E-V-S-P-I-N-Y) for both enzyme forms, and peptide mapping yielded 26 peptides that also appeared identical between the two enzyme forms. Studies on the nature of the association of the membrane enzyme form with the cell membrane suggest that this enzyme form does not represent the soluble form trapped during the enzyme preparation. It is suggested that the membrane form of the puromycin-sensitive aminopeptidase is identical to the soluble enzyme and that it associates with the membrane by interactions with other integral membrane proteins.     

Reactor design for minimizing product inhibition during enzymatic lignocellulose hydrolysis: II. Quantification of inhibition and suitability of membrane reactors

Product inhibition of cellulolytic enzymes affects the efficiency of the biocatalytic conversion of lignocellulosic biomass to ethanol and other valuable products. New strategies that focus on reactor designs encompassing product removal, notably glucose removal, during enzymatic cellulose conversion are required for alleviation of glucose product inhibition. Supported by numerous calculations this review assesses the quantitative aspects of glucose product inhibition on enzyme-catalyzed cellulose degradation rates. The significance of glucose product inhibition on dimensioning of different ideal reactor types, i.e. batch, continuous stirred, and plug-flow, is illustrated quantitatively by modeling different extents of cellulose conversion at different reaction conditions. The main operational challenges of membrane reactors for lignocellulose conversion are highlighted. Key membrane reactor features, including system set-up, dilution rate, glucose output profile, and the problem of cellobiose are examined to illustrate the quantitative significance of the glucose product inhibition and the total glucose concentration on the cellulolytic conversion rate. Comprehensive overviews of the available literature data for glucose removal by membranes and for cellulose enzyme stability in membrane reactors are given. The treatise clearly shows that membrane reactors allowing continuous, complete, glucose removal during enzymatic cellulose hydrolysis, can provide for both higher cellulose hydrolysis rates and higher enzyme usage efficiency (kg_product/kg_enzyme). Current membrane reactor designs are however not feasible for large scale operations. The report emphasizes that the industrial realization of cellulosic ethanol requires more focus on the operational feasibility within the different hydrolysis reactor designs, notably for membrane reactors, to achieve efficient enzyme-catalyzed cellulose degradation.     

Characterization of polymeric buffers for operating membrane-trapped enzyme reactors in an electric field

A novel class of amphoteric, polymeric buffers, is described, consisting of grafting onto growing polyacrylamide chains weakly acidic and basic acrylamido-monomers (called Immobilines; protolytic groups as N-substituents on the nitrogen of the amido bond), for operating a membrane-immobilized enzyme reactor (MIER) in an electric field. With these soluble, polymeric buffers, it is possible to operate the membrane reactor at any optimum of pH activity, for any given enzyme, in the pH 3-10 scale. Such buffers, being amphoteric, are confined in the enzyme reaction chamber by the same isoelectric trapping mechanism. The best buffers were found to be those polymerized in presence of 9% neutral monomer (acrylamide) and containing 20 mM Immobiline as buffering ion. To decrease their viscosity in solution, the polymeric buffers are synthesized at high temperatures (70 degrees C) and in presence of a chain-transfer agent. The weight average molecular size in these conditions has been found to be ca. 200,000 Da. These buffers exhibited excellent performance in a variety of enzyme reactions in the MIER, such as in the case of penicillin G acylase and histidine decarboxylase and were found to greatly stabilize enzyme activity, permitting operation of the MIER over extended periods of time. As an example, in a penicillin G acylase reactor, >75% enzyme activity was maintained over a 10-d cycle of operation, while with conventional buffers more than 90% inactivation was experienced over the same period of time. This novel class of macromolecular, amphoteric buffers could also be exploited in other types of conventional bioreactors not based on an isoelectric trapping mechanism.     

Enzymatic modification of vegetable protein: Immobilization of Penicillium duponti enzyme on reconstituted collagen and the use of the immobilized-enzyme complex for solubilizing vegetable protein in a recycle reactor

Penicillium duponti enzyme was immobilized on reconstituted collagen by macromolecular complication, impregnation, and covalent crosslinking techniques. The immobilization of the enzyme on collagen has a twofold purpose: (1) providing a protein microenvironment for the proteolytic enzyme; and (2) extending the useful life the enzyme once immobilized on the collagen matrix. Two types of collagen were used, one produced by the United States Department of Agriculture and the other produced by FMC. The USDA collagen contained unhydrolyzed telepeptide linkages and required pretreatment to reduce collagenaselike activity of the enzyme. Activity analysis of the immobilized enzyme complex showed that membranes with enzyme loading less than 10 mg enzyme/g of wet membrane in the reactor were dimensionally stable. The degree of crosslinking was an important parameter. Membranes with structural opening up to three times the initial dry thickness were found to be the maximum limit for controlled release of enzyme from the collagen membrane during enzymatic reaction. Higher activities and better stability of the enzyme in collagen membrane were found for covalent crosslinking of the enzyme to treated collagen films. The hydrolysis of soybean vegetable protein with the immobilized enzyme in a recycle reactor at enzyme loading of mg/g of wet membrane at 40°C, pH 3.4, produced 56.5% of soluble protein in 10h. The production is equivalent to 1.84 h total contact time between the substrate and the immobilized enzyme. The average productivity based on a stable enzyme activity and 20g of dry membrane was 329 mg of protein/g/mg of active enzyme immobilized. The productivity of the free enzyme in a batch reactor was 62.5 mg protein/h/mg enzyme.     

Roles of homooligomerization and membrane association in ATPase and proteolytic activities of FtsH in vitro.

Escherichia coli FtsH is a membrane-bound and ATP-dependent protease which degrades some soluble and integral membrane proteins. The N-terminal region of FtsH mediates membrane association as well as homooligomeric interaction of this enzyme. Previously, we studied in vivo functionality of FtsH derivatives, in which the N-terminal membrane region was either deleted (FtsH(DeltaTM)), replaced by a leucine zipper (Zip-FtsH(DeltaTM)), or replaced by a lactose permease transmembrane segment (LacY-FtsH). It was indicated that homooligomerization is required for the minimum proteolytic activity, whereas a transmembrane sequence is required for membrane protein degradation. Here we characterized these proteins in vitro. Although these mutant enzymes were very low in their activities, they were significantly stimulated by dimethyl sulfoxide, which enabled us to characterize their activities. LacY-FtsH degraded both soluble and membrane proteins, but Zip-FtsH(DeltaTM) only degraded soluble proteins. These proteins also exhibited significant ATPase activities. However, FtsH(DeltaTM) remained inactive both in ATPase and in protease activities even in the presence of dimethyl sulfoxide. The monomeric FtsH(DeltaTM) was able to bind ATP and a denatured protein. These results indicate that subunit association is important for the enzymatic catalysis by FtsH and that the additional presence of the transmembrane sequence is required for this enzyme to degrade a membrane protein even under detergent-solubilized conditions.