Enantioseparation of (R,S)-ketoprofen using Candida antarctica lipase B in an enzymatic membrane reactor

An enzymatic membrane reactor (EMR) for enantioseparation of (R,S)-ketoprofen via Candida antarctica lipase B (CALB) as biocatalyst was investigated. A comparative study of free and immobilized CALB was further conducted. The catalytic behaviour of CALB in an EMR was affected by the process parameters of enzyme load, substrate concentration, substrate molar ratio, lipase solution pH, reaction temperature, and substrate flow rate. Immobilization of CALB in the EMR was able to reduce the amount of enzyme required for the enantioseparation of (R,S)-ketoprofen. Immobilized CALB in the EMR assured higher reaction capacity, better thermal stability, and reusability. It was also found to be more cost effective and practical than free CALB in a batch reactor.     

A batch membrane reactor for laboratory studies

A membrane reactor consisting of two recirculating flow systems connected via a membrane module has been constructed and used to study the dehydrogenation of cyclohexane. When the reactor is operated differentially it is possible to obtain the same information that is generated when using more conventional steady flow reactors. The batch system has the advantages of easily varying the ratio of membrane area to reactor volume and sampling a very wide range of effective Damköhler numbers. These are important variables in design studies. This ability has been demonstrated for the dehydrogenation of cyclohexane. The batch system reproduced results from studies using a more conventional flow reactor. In addition, with the batch reactor it was possible to experimentally confirm predictions that were based upon computer simulation but which were outside the range of experimental study for the conventional reactors used.     

Physicochemical properties of cross-linked and acetylated starches and products of their hydrolysis in continuous recycle membrane reactor

The aim of the present work was to study the physicochemical properties of doubly modified, by cross-linking and acetylating, starches as well as the products of their enzymatic hydrolysis. A two step procedure of hydrolysis, including the batch and membrane reactors, were investigated. The second step of enzymatic processes were carried out in a continuous recycle membrane reactor (CRMR). Three kinds of commercial starches – two preparations of acetylated distarch adipate E1422 of different degrees of cross-linking, as well as one preparation of acetylated distarch phosphate E1414 were examined. It was found that the degree of substitution of acetyl groups in the macromolecules of starch did not influence the effectiveness of hydrolysis. However, the degree of cross-linking with adipate groups slightly decreased the efficiency of processing in the CRMR. Additionally, the relationship between the type of hydrocolloid and its adsorption activity in the air/water and oil/water systems was considered. All obtained derivatives revealed adsorption properties and reduced the surface/interface tension in the air/water and oil/water systems. The efficiency and effectiveness of adsorption of the investigated hydrocolloids were affected by the type of modification as well as the degree of substitution of acetyl groups in the macromolecules of starch. Particle size distributions formed in aqueous solutions for all investigated hydrolyses were determined and compared with results obtained for commercial products.     

Optimization of membrane area and catalyst distribution in a permeative-stage membrane reactor for methane steam reforming

Methane steam reforming to produce high purity hydrogen is conveniently carried out in membrane reactors. The interest on this process has led to several studies about the influence of the key operating variables on the system performances. In the present paper we focus on the optimization of the catalyst and membrane area axial distribution by computer simulation. To this purpose, a numerical model of a permeative-stage membrane reactor (PSMR), a system composed of traditional reactive and membrane permeative stages laid out in alternated series, has been developed. This is based on 1D mass, momentum and energy balances including thermal effects on all the system properties. First, an equi-sized nine-stage PSMR is analyzed at various temperatures and membrane thicknesses, in comparison with a conventional membrane reactor, showing that improved performances, especially in terms of methane conversion, can be obtained. Then, considering the stage lengths as design variables, the optimal system performances are determined by maximizing two objective functions, namely the methane conversion and the hydrogen recovery factor. Different optimal length distributions are found utilizing the two criteria, corresponding to privileged kinetic or permeative aspects. In comparison to the conventional MR, the PSMR leads to a higher conversion and lower recovery factor when the conversion is maximized, whilst the opposite situation occurs when maximizing the recovery factor. Furthermore, the role of the heat exchange area between the furnace and the reactor is studied, considering a PSMR with adiabatic permeative stages. From this case, it is possible to see that the greater advantage of this apparatus (having the same membrane area, catalyst amount and heat-exchange area as the MR) consists in a much higher recovery factor (+21% ca.), which at the end demonstrates to be the most convenient objective function by means of the introduction of an overall performance index, identified as the hydrogen recovery yield. Therefore, the analysis proposed in the present paper shows that the reactive/permeative stage distribution has to be considered an important reactor design parameter, which can be opportunely modified to improve the performances of the process.     

Phospholipase C-catalyzed sphingomyelin hydrolysis in a membrane reactor for ceramide production

A membrane reactor for the production of ceramide through sphingomyelin hydrolysis with phospholipase C from Clostridium perfringens was studied for the first time. Ceramide has raised a large interest as an active component in both pharmaceutical and cosmetic industry. The enzymatic hydrolysis of sphingomyelin has been proven to be a feasible method to produce ceramide. In the membrane reactor constructed, the aqueous phase and the organic phase were separated by a membrane containing the immobilized enzyme, while the organic phase was continuously circulated. Among the 10 selected membranes, the enzyme immobilized in membrane RC 70PP had low immobilization efficiency, but retained the highest catalytic activity. Three immobilization methods, i.e. filtration (adsorption/entrapment), covalent binding, and cross-linking, were compared. The enzyme immobilized by filtration had the highest activity even under the low fixation level (9.4%). The optimal flow rate of the organic phase was 5 ml/min. High initial enzyme amount in the immobilization led to the decrease in the fixation level. Both the initial reaction rate and the specific activity of the enzyme increased with increasing enzyme loading, and slightly decreased after the immobilized enzyme amount over 50 μg in 9.6 cm² membrane area. The immobilized enzyme retained 16% of the original activity after five cycles. Finally, the liquid enzyme, the enzyme immobilized on particle carriers, and the enzyme immobilized in the membrane were compared. The study demonstrated the improved enzyme reusability, the fast immobilization process, the straightforward up-scaling and the combination of the hydrolysis with the product separation in the membrane reactor developed.     

Investigation of enzymatic hydrolysis of lipid-like substrates in monolayers

The parameters of enzymatic hydrolysis of novel lipid-like substrates assembled in monolayers at water–air interface were estimated by a simple method. The method is based on measurement of the initial velocity of the reaction registered by the decrease of the monolayer area (caused by the enzymatic hydrolysis) at surface pressure of 10 mN/m in a single–compartment trough. Hydrolysis of trilaurin and three 1,3-dilaurylpseudoglycerides acylated by phenylalanine, leucine and valine was characterized by catalytic constants k_cat and apparent Michael's constants K_m(app) (using lipase from Pseudomonas fluorescens as catalyst). It was found that k_cat of the synthetic pseudoglycerides (7–13 per s) are higher than k_cat of trilaurin (4 per s) that can be explained by the presence of positively charged primary aminogroups in the substrates. K_m(app) values were found to be similar for all the substrates studied (ca. 2×10⁻⁶ M). The proposed method allows estimation of the kinetic constants in traditional dimensions.     

Perovskite membrane reactor for continuous and isothermal redox hydrogen production from the dissociation of water

The redox water splitting is one of the most promising routes for sustainable hydrogen production. Towards this goal, serious technological obstacles are set: (i) by the non-isothermal operation of the redox process, that causes serious reactor construction problems, and (ii) by the need for efficient high temperature oxygen/hydrogen separation technology which is a very challenging development. In this paper, perovskite materials having the formula La_0.3Sr_0.7FeO₃ were synthesized and subsequently tested for their high temperature oxidation/reduction behavior. The redox activity of the materials in relation to the water splitting reaction has been also investigated. Dense, disc shaped membranes of the materials were synthesized and placed in a membrane reactor. Experiments at 1133 K revealed the possibility of performing the reduction and oxidation steps simultaneously and isothermally on each side of the membrane reactor. A steady-state situation was thereby achieved where hydrogen was continuously produced on one side while the material was simultaneously regenerated on the other side. The created oxygen vacancy gradient formed the driving force for a continuous flux of vacancies from the membrane reduction surface to the membrane oxidation surface. The hydrogen production rate under the particular experimental conditions estimated to be ∼47.5 cm³ H₂ (STP) m⁻² min⁻¹. It could be increased by a factor of approximately 3, up to ∼145 cm³ H₂ (STP) m⁻² min⁻¹, if the membrane reduction was enhanced with a reductant such as carbon monoxide. This approach resulted in an efficient execution of the water gas shift reaction towards high purity hydrogen production.     

Modelling of enzymatic reaction in an internal loop airlift reactor

Gas-liquid reaction carried out in an internal loop airlift reactor was modelled and subjected to the scale-up procedure. Homogeneous oxidation of glucose to gluconic acid catalyzed by Gluzyme 10000 BG, a commercial product containing the enzymes glucose oxidase and catalase as active components, was chosen as the model system. The kinetic parameters were obtained using a 12-L airlift reactor considered as a CSTR. The behaviour of a large-scale internal loop airlift reactor was modelled dividing the reactor sections into a series of tank reactors. The reliability of the model was verified by comparing experimental measurements with the simulation results obtained employing 40-L and 200-L airlift reactors. The designed model could be suitable to predict the behaviour of large-scale internal loop airlift reactors. Presented at the 33rd International Conference of the Slovak Society of Chemical Engineering, Tatransk%e Matliare, 22–26 May 2006.     

Development of a membrane reactor for decomposing hydrogen sulfide into hydrogen using a high-performance amorphous silica membrane

We have successfully developed a membrane reactor for decomposing hydrogen sulfide into hydrogen using an amorphous silica membrane for the first time. The membrane was prepared by the CVD method with tetramethoxysilane and oxygen, and showed excellent hydrogen permeance at 873 K of the order of 10⁻⁷ mol m⁻² s⁻¹ Pa⁻¹ and high hydrogen/nitrogen permselectivity of 10⁴. The membrane reactor constructed with our membrane and a commercially available catalyst decomposed hydrogen sulfide into hydrogen with higher conversion than the equilibrium conversion. This conversion enhancement was because of the selective extraction of hydrogen from the reaction side to the permeate side by the silica membrane.     

Modeling of enzymatic reaction in an airlift reactor using an axial dispersion model

This work was focused on modeling of biochemical processes in a 40-L internal-loop airlift reactor. Due to different mixing in the specific zones of the reactor four main sections, bottom, riser, separator and downcomer, were recognized. Each zone was modeled by an adequate mixing model: bottom and separator sections by the model of ideally-stirred reactor; riser and downcomer sections by the model of plug-flow reactor with axial dispersion. In the model, the effects of mass transfer, hydrodynamics, and reaction kinetics were taken into account. The model of the reactor was experimentally verified by the aerobic enzymatic oxidation of glucose to gluconic acid. Simulations are in good agreement with experimental data. Presented at the 34th International Conference of the Slovak Society of Chemical Engineering, Tatranské Matliare, 21–25 May 2007.     

Use of a membrane reactor to improve selectivity to intermediate products in consecutive catalytic reactions

Through modeling it has been shown that a concentric-tube catalytic membrane reactor can be used to increase the selectivity for the intermediate products of a consecutive reaction scheme. The reactants are fed to the tube-side of the reactor where the catalyst is also located. The wall of the tube is permeable, allowing the intermediate products to pass through to the annular space instead of undergoing further reaction. The annular space is swept by an inert gas flow and contains no catalyst. Both permselective and non-permselective membranes have been considered in both co-current and counter-current flow regimes. In contrast to most catalytic membrane reactor applications where reactions are reversible and thermodynamically limited, in the present study the reactions considered are irreversible and are under kinetic control.     

Oxygen permeation and oxidative coupling of methane in membrane reactor: A new facile synthesis method for selective perovskite catalyst

A dense membrane of La_0.6Sr_0.4Co_0.8Fe_0.2O_3−δ (LSCF) perovskite was prepared by a new chelating agent, ethylene diamine N,N,N′,N′-tetra N-acetyl diamine (EDTNAD). As a potent ligand, EDTNAD provided a facile one-step method to form complexes of the four metal ions, simultaneously. The oxygen permeation flux through the pure perovskite LSCF dense membrane was measured over temperature range of 1073–1223 K, thickness of 0.7–1.0 mm and oxygen partial pressure of 0.1–1.0 bar. Oxidative coupling of methane (OCM) reaction using LSCF disk in the atmospheric membrane reactor and over the temperature range of 1073–1173 K showed a C₂ selectivity of 100% and C₂ yield of 5.01% at 1153 K. Furthermore, OCM reaction data of the membrane reactor were discussed and compared with those of the fixed bed using the same perovskite powder as the catalyst.     

The structural changes in crystalline cellulose and effects on enzymatic digestibility

The enzymatic hydrolysis of cellulose I achieves almost complete digestion when sufficient enzyme loading as much as 20 mg/g-substrate is applied. However, the yield of digestion reaches the limit when the enzyme dosage is decreased to 2 mg/g-substrate. Therefore, we have performed three pretreatments such as mercerization, dissolution into phosphoric acid and EDA treatment. Transformation into cellulose II hydrate by mercerization and dissolution into phosphoric acid were not sufficient because substrate changed to highly crystalline structure during saccharification. On the other hand, in the case of crystalline conversion of cellulose I to III_I by EDA, almost perfect digestion was achieved even in enzyme loading as small as 0.5 mg/g-substrate, furthermore, hydrolyzed residue was typical cellulose I. The structural analysis of substrate after saccharification provides an insight into relationships between cellulose crystalline property and cellulase toward better enzymatic digestion.     

Metal bioavailability in marine sediments measured by chemical extraction and enzymatic mobilization

In this work we compared metal bioavailable fractions in marine sediments operationally measured by sequential selective extractions (in particular the labile fraction released by acetic acid) and by a biomimetic approach using a commercially available proteolytic enzyme, proteinase K, chosen because of its non-specific behaviour and because it is representative of the enzymes encountered in many deposit-feeding organisms. Different experimental conditions for enzymatic extraction were investigated and the enzyme was employed both untreated and thermally denatured to study metal release mechanisms (i.e. enzymatic hydrolysis and/or complexation). Extractable protein content was also measured to verify possible correlations with some metals.Considering the two sediments used in this work, the available fraction evaluated with a biomimetic approach was often significantly lower than the fraction released by the first step of selective extractions, as expected. Moreover a good correlation was found between the fraction of metal available to the enzyme and enrichment factors in the gut fluids of deposit-feeding organisms, suggesting that enzymatic approach is qualitatively more reliable than chemical extraction in replicating the mechanism of metal mobilization that occurs in the guts of deposit-feeders.     

The determination of phenol in urine by enzymatic hydrolysis/headspace gas chromatography

Summary A new method has been developed for the determination of phenol in urine in which the phenol conjugates are hydrolysed enzymatically and the liberated phenol is analysed by headspace chromatography. The results compare favourably with those obtained by the method of van Haaften and Sie in which acid hydrolysis is carried out in a heated GC precolumn. The enzymatic hydrolysis headspace technique appears to be very reliable and does not suffer from the disadvantages of precolumn acid hydrolysis.Since this paper was submitted, we have found a report on the enzymatic hydrolysis of phenyl glucuronide in urine followed by gas chromatographic analysis which seems to have been overlooked by later workers. The paper is by H. Desoille, T. F. Gandenzi-Britto and M. Philbert in Archives des Maladies Professionelles, de Medecine du Travail et de Securite Sociale (Paris),30 (3), 129 (1969).     

Effect of inhibitors released during steam-explosion pretreatment of barley straw on enzymatic hydrolysis

The influence of the liquid fraction (prehydrolysate) generated during steam-explosion pretreatment (210°C, 15 min) of barley straw on the enzymatic hydrolysis was determined. Prehydrolysate was analyzed for degradation compounds and sugars' content and used as a medium for enzymatic hydrolysis tests after pH adjusting to 4.8. Our results show that the presence of the compounds contained in the prehydrolysate strongly affects the hydrolysis step (a 25% decrease in cellulose conversion compared with control). Sugars are shown to be more potent inhibitors of enzymatic hydrolysis than degradation products.     

Syngas production in a novel perovskite membrane reactor with co-feed of CO2

Partial oxidation of methane（POM） co-fed with CO₂ to syngas in a novel catalytic BaCo_0.6Fe_0.2Ta_0.2O_3-δ oxygen permeable membrane reactor was successfully reported.Adding CO₂ to the partial oxidation of methane reaction not only alters the ratio of CO/H₂,but also increases the oxygen permeation flux and CH₄ conversion.Around 96%CH₄ conversion with more than 93%CO₂ conversion and 100%CO selectivity is achieved,which shows an excellent reaction performance.A steady oxygen permeation flux of 15 mL/（cm² min） is obtained during the 100-h operation,which shows good stability as well.     

An enzymatic approach to the cleaning of ultrafiltration membranes fouled in abattoir effluent

Membrane fouling severely curtails the economical and practical implementation for the purification of biologically related process streams such as abattoir effluent (Jacobs, WRC Report no. K5/362, 1991, Pretoria, South Africa [1]). Mechanical and chemical removal of foulants usually lead to membrane damage and additional pollution. Enzymes, specific for the degradation of proteins and lipids, were tested as key components of biological cleaning regimes for membranes fouled in abattoir effluent. Fouling of polysulphone membranes was assessed as previously described by Maartens et al. (J. Membrane Sci., 119 (1996) 1 [2]) and optimal enzyme concentrations and incubation times were determined for the different preparations. The ability of each cleaning agent to remove adsorbed protein and lipid material, as well as their ability to restore the water-contact angle and the pure-water flux of the fouled membranes, were determined and compared. These variables were also used to compare the cleaning efficiency of enzymatic cleaning agents with conventional chemical agents under optimal conditions. The enzymes and enzyme detergent mixtures were effective cleaning agents and the pure-water flux of statically fouled membranes could be restored by treatment with these agents.     

Influence of mixing regime on enzymatic saccharification of steam-exploded softwood chips

In an attempt to elucidate the effect of reduced mixing on the enzymatic hydrolysis of lignocellulosic feedstocks, a pretreated softwood substrate was hydrolyzed under various mixing regimes using a commercial cellulase mixture. The substrate was generated by SO₂-catalyzed steam explosion of Douglas fir wood chips followed by alkali-peroxide treatment to remove lignin. Three mixing regimes were tested; continuous mixing at low (25 rpm) and high (150 rpm) speeds, and mixing at low-speed interspersed with 5-min intervals of high-speed agitation at 150 rpm. At both substrate concentrations (7.5 and 10% [w/w]), the mixed-speed mixing was able to produce sufficiently high conversion rates and yields (93% after 96 h), close or slightly better than those obtained under vigorous mixing (150 rpm). The low-speed shaking produced appreciably lower conversion yields at both levels of substrate concentration. Therefore, the mixed-speed regime may be a viable process option, because it does not seem to have an adverse impact on the cellulose conversion yield and can be an effective means of reducing the mixing energy requirements of an enzymatic hydrolysis process.     

Flow injection analysis of angiotensin I-converting enzyme inhibitory activity with enzymatic reactors

Assay of angiotensin I-converting enzyme (ACE) inhibitory activity always draws much attention because of diverse applications in the field of antihypertension and related pathogenesis. Recently, the use of a new synthetic substrate, 3-hydroxybutyrylglycyl-glycyl-glycine (3HB-GGG), for the assay of ACE inhibitory activity has been confirmed. To construct a rapid, economical, and automatic determination system of ACE inhibitory activity using 3HB-GGG, a flow injection analysis (FIA) system with enzymatic reactors was developed in this study. Enzyme reactors were composed of aminoacylase and 3-hydroxybutyrate dehydrogenase immobilized separately on CNBr-activated Sepharose 4B. The assay condition was optimized in terms of the conversion of 3HB-G into NADH by the enzymatic reactors when the reaction solution containing 3HB-G generated from 3HB-GGG (after the incubation with ACE) was repetitively injected into the FIA system. Under the optimized conditions, 3HB-G was converted to 3HB, and then 3HB was oxidized by NAD⁺ to form NADH. The developed system successfully detected practical ACE inhibitors with a great sensitivity, high sampling frequency (10 samples h⁻¹) and a durable stability of the enzymatic reactors.