Lipase-catalyzed optical resolution of racemic naproxen in biphasic enzyme membrane reactors

A lipase-immobilized membrane reactor was applied for the optical resolution of racemic naproxen, and the effect of various operation conditions on reaction rate and enantio-selectivity was examined. The membrane reactor consisted of an organic phase dissolving naproxen ester, a lipase-immobilized polyamide membrane, and an aqueous phase to recover the reaction products. The lipase immobilized in the membrane reactor showed a stable activity for more than 200 h of continuous operation, while the native lipase in emulsioned stirred tank reactor quickly lost its activity showing an half-life time of about 2 h. When crude lipase was used, the biphasic enzyme membrane reactor gave smaller enantio-selectivity compared to the native lipase in the emulsioned tank reactor, whilst the use of pure lipase gave similar results to the native lipase. This paper discusses that other hydrolases present in the crude enzyme powder caused the decrease of enantio-selectivity. Enantio-selectivity depended on the substrate concentration, amount of enzyme loaded in the membrane and immobilization site. In fact, these parameters affect the organic/aqueous interface that plays an important role in the enhancement of enantio-selectivity.     

Preparation of PVDF porous membranes by using PVDF-g-PVP powder as an additive and their antifouling property

The hydrophilic PVDF-g-PVP powder was used as additive to prepare a series of PVDF/PVDF-g-PVP blend porous membranes via an immersion precipitation phase inversion process. FTIR-ATR measurements confirmed that the hydrophilic PVP preferentially segregated to the interface between membrane and coagulant. SEM images showed that there was no big change in the membrane cross-section with the amount of PVDF-g-PVP increased. However, the membrane surface roughness increased with the amount of PVDF-g-PVP increased according to AFM data. The mean pore size of membranes reached max when the amount of PVDF-g-PVP was 10 wt%. The water contact angle and filtration experiments revealed that the surface enrichment of PVP endowed the membranes with significantly enhanced surface hydrophilicity and protein-adsorption resistance. The flux recovery of the porous membranes was increased from 37.50% to 77.23% with the amount of PVDF-g-PVP increased from 0 to 50 wt%, also indicating that the antifouling property of the porous membranes was improved.     

The effect of sodium dodecyl sulfate solutions as gelation media on the formation of PES membranes

Sodium dodecyl sulfate (SDS) aqueous solutions were used as gelation media in the preparation of polyethersulfone (PES) membranes. The casting solution composition was the same for all the tested membranes. The temperatures of gelation media were 4 and 20°C. The concentration of SDS was changed from 0 to 3.0 g/l at 4°C and 0 to 1.6 g/l at 20°C.The surface tension of the gelation media was measured by drop weight method and the electrical conductivities were also determined. The membranes were characterized by transport parameters obtained from separation experiments and roughness parameters, obtained by the atomic force microscopic (AFM) technique.The molecular weight cut-off (MWCO) values of the studied membranes were found to be between 9 000 and 88 000 Da for membranes gelled at 4°C, and between 28 000 and 85 000 Da for membranes gelled at 20°C. The pore sizes were found to be between 3.04 and 10.73 nm for the membranes gelled at 4°C and between 4.48 and 10.74 nm for membranes gelled at 20°C, respectively. In general, both MWCO and pore size decreased with an increase of SDS concentration in gelation media when the concentration was below critical micelle concentration (CMC) and increased with an increase with SDS concentration when the concentration was above CMC. Images of membrane surfaces, taken by AFM, showed that the size of nodules and depressions decreased with a decrease in pore size. The roughness of membranes increased with an increase in pore size and MWCO.     

Characterization of non-uniformly charged ion-exchange membranes prepared by plasma-induced graft polymerization

Cation-exchange membranes were prepared by plasma-induced grafting of sulfonated glycidyl methacrylate (GMA) and porous polypropylene (PP) membranes. The chemical and physical structures of the prepared membranes were investigated using Fourier transform infrared spectroscopy (FTIR), field emission-scanning electron microscopy (FESEM) and electron-probe micro-analyzing (EPMA). The membranes were also characterized in terms of their electrochemical properties. A non-uniform distribution of fixed charges across the membrane matrix was detected by EPMA analysis. This non-uniform distribution of the fixed charges is the result of using water as solvent for the monomer which led to a fast reaction on the membrane surface and a slow diffusion of the monomer into the pores of the membrane. The prepared membranes exhibited moderate ion-exchange capacities (2.53–3.30 mmol/g dry membrane) and electrical resistances (0.349–0.589 Ω cm²) and an ion permselectivity comparable to that of the commercial membrane CM-1 (Tokuyama Corp.), while the water content of the membranes was significantly higher than that of the commercial membrane. The higher water content of the membranes is the result of water occupying the pores in the bulk of the support membrane after the dense layers with fixed charges are formed on the membrane surfaces by the grafting reaction. The relatively high ion permselectivity in spite of the high water sorption of the membranes is the result of the high fixed charge density in the layers on the membrane surfaces. Current versus voltage curves and the chronopotentiometric measurements revealed that the sulfonated GMA-g-PP membranes can be operated effectively at high current density.     

Characterisation of membrane surfaces: direct measurement of biological adhesion using an atomic force microscope

An atomic force microscope (AFM) in conjunction with coated colloid probe and cell probe techniques has been used to measure directly the adhesive force between both the protein bovine serum albumin (BSA) and a yeast cell at two different membranes. These were polymeric ultrafiltration membranes of similar MWCO (4000 Da) but of different materials (ES 404 and XP 117, PCI Membrane Systems, UK). The XP 117 membrane is made from a mixture of polymers chosen with the aim of achieving low fouling. The BSA was adsorbed on a 5 μm silica colloid probe formed from a tipless V-shaped AFM cantilever. The cell probe was created by immobilising a single yeast cell on such a tipless cantilever. Measurements were made in 10⁻² M NaCl solution. It was found for both protein and cell systems that the adhesive force at the ES 404 membrane was greater than that at the XP 117 membrane. The paper shows that coated colloid probe and cell probe techniques can provide useful means of directly quantifying the adhesion of biological materials to membrane surfaces.     

Preparation and characterization of porous conducting poly(dl-lactide) composite membranes

Solid conducting biodegradable composite membranes have shown to enhance nerve regeneration. However, few efforts have been directed toward porous conducting biodegradable composite membranes for the same purpose. In this study, we have fabricated some porous conducting poly(dl-lactide) composite membranes which can be used for the biodegradable nerve conduits. The porous poly(dl-lactide) membranes were first prepared through a phase separation method, and then they were incorporated with polypyrrole to produce porous conducting composite membranes by polymerizing pyrrole monomer in gas phase using FeCl₃ as oxidant. The preparation conditions were optimized to obtain membranes with controlled pore size and porosity. The direct current conductivity of composite membrane was investigated using standard four-point technique. The effects of polymerization time and the concentration of oxidant on the conductivity of the composite membrane were examined. Under optimized polymerization conditions, some composite membranes showed a conductivity close to 10⁻³ S cm⁻¹ with a lower polypyrrole loading between 2 and 3 wt.%. A consecutive degradation in Ringer's solution at 37 °C indicated that the conductivity of composite membrane did not exhibit significant changes until 9 weeks although a noticeable weight loss of the composite membrane could be seen since the end of the second week.     

Effect of aging on UF membranes by a streaming potential (SP) method

In this paper we have determined, by a streaming potential (SP) method, the isoelectric point (IEP) of a new cellulose membrane, the regenerated cellulose material. This membrane is more hydrophilic than the classical cellulose acetate material and less sensitive to protein adsorption, with an IEP of 3.4.Furthermore, we have validated an SP method as a new method to control aging of porous membranes. We validate the SP technique on a surface of 30 cm² for a membrane with a molecular weight cut-off of 10 kDa.In this new field of research where nondestructive techniques are not many, we have shown, for the first time, the efficiency of coupling permeability and SP measurements to control aging of mesoporous polymer membranes.     

Direct visual observation of yeast deposition and removal during microfiltration

Periodic reverse flow through membranes is an effective technique to remove foulants from microfiltration (MF) membrane surfaces. This work explored direct visual observation (DVO) of yeast deposition and subsequent removal via backwashing and single backpulses using microvideo photography with cellulose-acetate (CA) and Anopore anodised-alumina (AN) MF membranes. Foulant deposited less uniformly on the surfaces of the CA membranes than on the AN membrane surfaces during forward filtration. Foulant cake layers of approximately 30 μm thickness formed on both membranes after forward filtration for 1–2 h, leading to fouled-membrane fluxes of only 15–25% of the clean-membrane fluxes.Foulant was removed by reverse flow from the CA membrane surfaces in clumps. The time constant for foulant removal was determined from photomicrographs to be approximately 0.2 s, and 95% of the membrane surface was cleaned within 1 s of backpulsing, resulting in 95% recovery of the initial flux. The foulant cake was also removed from the AN membranes in clumps, though much of the membrane remained covered in a monolayer of yeast. The flux through the membrane covered with a full monolayer was determined during forward filtration to be about 70% of the clean membrane flux.A model for flux recovery is proposed which takes into account the fraction of the membrane surface which is completely cleaned as well as the fraction which remains covered in a foulant monolayer. The predicted and experimentally-determined recovered fluxes as a function of backpulse duration are in very good agreement.     

Membrane characterization by solute transport and atomic force microscopy

Various ultrafiltration and nanofiltration membranes were characterized by solute transport and also by atomic force microscope (AFM). The molecular weight cut-off (MWCO) of the membranes studied were found to be between 3500 and 98,000 Daltons. The mean pore size (μ_p) and the geometric standard deviation (σ_p) around mean ranged from 0.7 to 11.12 nm and 1.68 to 3.31, respectively, when calculated from the solute transport data. Mean pore sizes measured by AFM were about 3.5 times larger than calculated from the solute transport. Pore sizes measured by AFM were remarkably fitted to the log-normal probability distribution curve. Pore sizes of the membranes with low MWCO (20,000 Daltons and lower) could not be measured by AFM because of indistinct pores. In most cases, the pore density ranged from 38 to 1291 pores/μm². In general, the pore density was higher for the membrane having lower MWCO. Surface porosity was around 0.5–1.0% as measured from the solute transport and was 9.5–12.9% as obtained from AFM images. When membranes were coated with a thin layer of sulfonated polyphenylene oxide, mean pore sizes were reduced for all the membranes. Surface roughness was also reduced on coating.     

Macroporous chitin affinity membranes for wheat germ agglutinin purification from wheat germ

Macroporous chitin membranes of controlled porosity and pore sizes have been prepared. They have good mechanical properties and allow high flow rates of protein solutions at low pressure drops. Because of the numerous N-acetyl-D-glucosamine (GlcNAc) moieties they contain, the chitin membranes can be used for the separation of some valuable proteins both as affinity ligands and support matrix, without further modification. Due to their high porosity and high adsorption surface area, the chitin membranes provide a larger number of accessible binding sites for the wheat germ agglutinin than the chitin beads do. The adsorption capacity for wheat germ agglutinin (180 mg/g chitin membrane) is about 20 times larger than that of chitin beads. Because of the numerous binding sites, multiple-point bindings are involved in the protein adsorption. For this reason, a strong eluant, namely a 1 M acetic acid aqueous solution, had to be used to efficiently recover the wheat germ agglutinin from the membrane. The wheat germ agglutinin was extracted from wheat germ with 0.05 M HCl, precipitated with ammonium sulfate, dialyzed against 0.01 M Tris–HCl buffer (pH 8.5), and purified on the chitin membrane. A high purity (>99%) wheat germ agglutinin with high yield (∼50 mg/100 g wheat germ) was obtained.     

A comparison of lipase and trypsin encapsulated in mesoporous materials with varying pore sizes and pH conditions

Immobilized enzymes have an advantage over enzymes free in solution in that they are easily recovered after completed reaction. In addition, immobilization often gives enhanced stability. Entrapment of an enzyme in the pores of a mesoporous material is an attractive procedure since the enzyme is immobilized without any covalent bonding to a support which may be detrimental to the catalytic performance. The objective of this work is to compare the encapsulation and catalytic performance of lipase from Mucor miehei and trypsin from bovine pancreas, two hydrolases with rather dissimilar properties and structures. We also demonstrate the importance of the pore dimensions and the pH for proper function of the encapsulated enzyme. Mesoporous silica particles (SBA-15) with three different pore sizes (50 Å, 60 Å and 89 Å) were synthesized and hexagonal structures with narrow pore size distributions were confirmed with TEM, SAXS and N₂-adsorption. Lipase and trypsin were encapsulated separately in the silica particles and the results indicate distinct differences between the two enzymes, both in loading capacity and catalytic activity. For trypsin the encapsulation rate and the loading capacity were large with a maximum reached at pH 7.6. The largest product yield was obtained with the particles with 60 Å pores, however, the yield was significantly lower than with free trypsin. For lipase optimal encapsulation rate and loading capacity were reached with the particles with 89 Å pores at pH 6.0 but were low compared to trypsin. However, the catalytic activity of the encapsulated lipase was more than twice as large as for free lipase, which can be explained by an interfacial activation of lipase at the silica surface.     

High-speed recovery of antimony using chelating porous hollow-fiber membrane

A porous hollow-fiber membrane containing an iminodiethanol (IDE) group as the chelate-forming group was applied to the recovery of antimony in the permeation mode. An antimony solution was forced to permeate through the pores of the chelating porous hollow-fiber membrane, driven by a transmembrane pressure. The membrane with a thickness of 0.7 mm and a porosity of 70% had an iminodiethanol group of 1.6 mol/kg of the membrane and a water flux of 0.95 m/h at 0.1 MPa and 298 K. The breakthrough curves of antimony overlapped irrespective of the permeation rate of the antimony solution ranging from 2 to 20 ml/min, i.e. the residence time across the membrane thickness ranging from 3.4 to 0.34 s, because of negligible diffusional mass-transfer resistance of the ionic species of antimony to the iminodiethanol group. At antimony concentrations below 10 mg/l (pH 4.0), a linear adsorption isotherm was obtained. The adsorbed antimony was quantitatively eluted by permeation of 2 M hydrochloric acid through the pores of the membrane.     

Nanopatterning of Si(1 1 1) surfaces by atomic force microscope scratching of an organic monolayer

In this work, we demonstrate selective electroless deposition of Cu into nanoscratches produced on n-type Si(1 1 1) surfaces covered with an organic monolayer. The organic layer (undecylenic acid) was covalently attached to a hydrogen-terminated Si surface. The nanosize scratches were produced with an atomic force microscope (AFM) in contact mode using a diamond-coated tip. Copper was deposited in the scratched regions with an electroless (immersion plating) approach using a 0.05 M CuSO₄ + 1% HF electrolyte. The results show clearly that the organic layer can be used as a mask for the deposition of Cu. Optimization of the electrochemical parameters, leads to a very high selectivity and uniform and well-defined nanostructures. This process represents a novel approach for a direct patterning of Si surfaces using an immersion plating reaction.     

Albumin separation with Cibacron Blue carrying macroporous chitosan and chitin affinity membranes

Cibacron Blue F3GA, Procion Red HE-3B and Procion Blue MX-R were immobilized on macroporous chitosan and chitin membranes with concentrations as high as 10–200 μmol/ml membrane. These dyed membranes were chemically and mechanically stable, could be reproducibly prepared, and operated at high flow rates. Human serum albumin (HSA) and bovine serum albumin (BSA) were selected as model proteins, and their adsorption on and desorption from the dyed chitosan membranes investigated. The Cibacron Blue F3GA membranes had a higher protein adsorption capacity, much greater for HSA than BSA, than the other dyed membranes. About 8.4 mg HSA/ml membrane were adsorbed at saturation by Cibacron Blue F3GA–chitosan membranes from a 0.05 M Tris–HCl/0.05 M NaCl, pH 8 solution. The chitin membranes had a lower dye content and hence a lower protein adsorption capacity than the chitosan membranes. The effects of important operation parameters (flow rate, protein concentration and loading) were also investigated. Cibacron Blue F3GA–chitosan membranes were employed for the separation of HSA from human plasma and high purity HSA thus obtained. This suggests that these membranes could be used for large-scale plasma fractionation.     

Alumina ultrafiltration membranes derived from carboxylate–alumoxane nanoparticles

The fabrication of asymmetric alumina ultrafiltration membranes using acetic acid surface stabilized alumina nanoparticles (A-alumoxanes) has been investigated. Contacting α-alumina supports with an aqueous solution of A-alumoxane (after firing to 1000°C) yields a defect free alumina membrane with a thickness of ca. 2 μm. The alumoxane-derived membranes have a molecular weight cut-off in the range of 35,000–44,000 g mol⁻¹, high porosity, and a permeability that is comparable to or greater than that of commercially available alumina membranes. SEM and AFM show that the surface of the alumoxane-derived membranes is quite smooth and contact angles show that the membrane is hydrophillic. A comparison with commercial alumina and polymer membranes, as well as those derived from sol–gel methods is presented.     

Hollow-fiber-type pore-filling membranes made by plasma-graft polymerization for the removal of chlorinated organics from water

Hollow-fiber-type pore-filling membranes were prepared to reduce the emission of toxic chlorinated organics into the environment. These membranes can remove 1,1,2-trichloroethane (TCE) or dichloromethane (DM) from water, and concentrate them in the permeate. The pore-filling membrane can efficiently remove organics from water because of the suppression of the membrane swelling by the porous substrate matrix, and the fact that it can maintain a high solute diffusivity, because of the linear graft chains that fill the substrate pores. Laurylacrylate (LA) or n-butylacrylate (BA) grafted layers were formed inside the porous hollow-fiber substrate, and the pores were filled with the grafted chains formed from plasma-initiated graft polymerization. The hollow-fiber-type LA-grafted membranes showed extremely high separation properties: a 0.09 wt.% TCE aqueous solution was condensed to 99 wt.% TCE in the permeate. The membrane can remove TCE from a water stream, and at the same time, the membrane can purify the TCE for re-use. The membrane also showed high separation performance for an aqueous DM solution. The mass transfer resistance outside the membrane was estimated by using a concentration polarization model. When the mass transfer coefficient at the membrane and feed stream boundary layer was below 10⁻⁴ m/s, the boundary layer resistance affected the membrane performance. This needs to be taken into account when designing the membrane module and operating conditions.     

Polysulfone — sulfonated poly(ether ether) ketone blend membranes: systematic synthesis and characterisation

The effect of sulfonated poly(ether ether ketone) (SPEEK) in membrane formation and separation properties has been investigated in polysulfone(PSU)/SPEEK/N-methyl-2-pyrrolidinone (NMP) systems. Charged ultrafiltration/nanofiltration membranes were obtained reliably in the range of 0.5–5 wt.% SPEEK in the polymer blend. All PSU/SPEEK blend membranes had substantially higher water flux, salt rejection, porosity and greatly reduced particle adhesion compared to the PSU base membrane. Further, all of these properties varied systematically with variation of SPEEK content. Reproducibility and stability of the membrane properties was excellent. Pore sizes determined from dextran retention data and AFM measurements showed reasonable agreement. Membranes with 5 wt.% SPEEK demonstrated excellent overall properties. Such membranes had very high permeability, 22.6±1.6×10⁻¹¹ m³ s⁻¹ N⁻¹, 0.999 fractional rejection of 4000 Da dextran, 0.65 rejection of 0.001 M NaCl, and only 0.75 mN m⁻¹ adhesion of a 4 μm silica particle. Such membranes are very promising for scale-up of production and testing on real process streams.     

Ultrathin self-assembled polyelectrolyte membranes for pervaporation

Ethanol–water pervaporation through new composite membranes with ultrathin self-assembled polyelectrolyte separating layer is described. The composite membranes were prepared by alternating electrostatic adsorption of poly(allylamine hydrochloride) (PAH) and poly(styrene sulfonate sodium salt) (PSS) on a porous PAN/PET supporting membrane (a polyethylene terephthalate fleece coated with a thin layer of polyacrylonitrile). The sealing of the pores of the supporting membrane was studied by gas flow measurements. Pervaporation experiments were carried out under variation of the preparation and operation conditions. Generally it was found that the separation capability considerably increased, when the composite membrane was annealed at temperatures above 60°C, while the flux simultaneously decreased. The same was found, when the number of PAH/PSS layers was increased. Raising the pervaporation temperature led to both an increase of the flux and the separation factor. The highest separation factor of 70 was found at a low water content of the feed of 6.2% (w/w). The corresponding flux was 230 g m⁻² h⁻¹. Pervaporation was feasible up to a water content of 24% (w/w) in the feed. At higher values, hydrolysis set in resulting in partial desorption of the separating layer.     

Polyaniline nanotubes for impedimetric triglyceride detection

Polyaniline nanotubes (PANI-NT) based film electrophoretically deposited onto indium–tin–oxide (ITO) coated glass plate has been utilized for covalent immobilization of lipase (LIP), via glutaraldehyde (Glu), for triglyceride detection using impedimetric technique. It is shown that fatty acid molecules produced during triglyceride hydrolysis result in change in charge transfer resistance (R_CT) of PANI-NT film with varying triglyceride concentration. LIP/Glu/PANI-NT/ITO bioelectrode has linearity as 25–300 mg dL^?1, sensitivity as 2.59 × 10^?3 KΩ^?1 mg^?1 dL, response time as 20 s and regression coefficient as 0.99. A low value of apparent Michaelis–Menten constant (～0.62 mM) indicates high enzyme affinity to tributyrin. The LIP/Glu/PANI-NT/ITO bioelectrode has been utilized to estimate triglyceride in serum samples.     

Comparison of <Emphasis Type="Italic">Yarrowia lipolytica</Emphasis> Lipase Immobilization Yield of Entrapment,Adsorption, and Covalent Bond Techniques

The purpose of this study was to immobilize lipase from Yarrowia lipolytica using three methods including inclusion, adsorption, and covalent bond to study enzyme leaching, storage, and catalytic properties. Sodium alginate and chitosan were the polymers selected to immobilize lipase by inclusion. The beads of each polymer were dried by freeze drying and fluidization. The results show that chitosan was more adapted to the inclusion of lipase. Even though freeze dried, bead activity was low compared to that of fluidized beads. The freeze-drying process seems to produce suitable beads for storage at 4 and 20 degrees C. The immobilization by adsorption was carried out on both celite and silica gel. Maximum immobilization yield of 76% was obtained with celite followed by 43% in silica gel. The enzyme adsorbed on the two supports exhibited greater stability at a certain temperature (50 degrees C) and in no polar solvents (Isooctane, n-heptane, and n-hexane). In addition, the lipase immobilized by covalent bond retained residual activity equitable to 70%. It was demonstrated that the enzyme immobilized by covalent bond showed greater activity (80%) after 5 months of storage.