Monitoring biotransformations in polyamide fibres

The enzymatic hydrolysis of polyamide fibres yields amino and carboxylic groups. These groups can be found in solution treatments as polyamide monomers and soluble oligomers. The amino groups can also be found at the surface of the fibres as end group chains. In this paper we report two methods to quantify the formation of these groups as a result of the enzymatic action. Soluble amino groups can be quantified with 2,4,6-trinitrobenzenesulfonic acid (TNBS), which yields a coloured complex which can be determined spectrophotometrically. The amino groups on the fibre surface can be quantified by reaction with a wool reactive dye and determination of colour intensities after a dyeing procedure below the glass transition temperature of polyamide.     

Light emitting diode-based algal photobioreactor with external gas exchange

Regeneration of atmosphere is an essential component in a long-term manned mission in space. A compact and reliable photobioreactor (PBR) system with an efficient gas transfer module is required for this purpose. Light emitting diodes (LEDs) provide an ideal light source for a small and maintenance-free PBR. Lack of gravity in space prevents the use of sparging, one of the most efficient gas exchange processes. As an alternative gas transfer device, a hollow fiber gas exchanger was selected and examined for possible future application. An LED-based PBR with a hollow fiber external gas exchanger supported high-density algal cultures comparable to a PBR with internal sparging (>2×10⁹cells/ml, or over 6% v/v). The growth kinetics in both types of PBRs were found to be identical and the oxygen production rate was about the same when the effect of the dark volume in the external hollow fiber gas exchanger was taken into account. To quantitatively describe the effect of non-illuminated volume inside a hollow fiber gas exchange unit, two parameters were introduced: ϵ, which was the ratio of illuminated volume to dark volume in the entire PBR system, and Φ, defined as the ratio of the specific dark respiration rate to the maximum specific oxygen production rate. The decrease in net oxygen production in a PBR with an external gas exchanger was quantitatively predicted by a simple model using these two parameters.     

Discontinuous membrane helices in transport proteins and their correlation with function

Alpha-helical bundles and beta-barrel proteins represent the two basic types of architecture known for integral membrane proteins. Irregular structural motifs have been revealed with the growing number of structures determined. "Discontinuous" helices are present in membrane proteins that actively transport ions. In the Ca(2+)-ATPase, a primary active transporter, and in the secondary transporters NhaA, LeuT(Aa), ClC H(+)/Cl(-) exchanger and Glt(Ph), the helical structure of two membrane segments is interrupted and the interjacent polypeptide chain forms an extended peptide. The discontinuous helices are integrated in the membrane either as transmembrane-spanning or hairpin-type segments. In addition, the secondary transporters have inverted internal duplication domains, which are only weakly correlated with their amino acid sequence. The symmetry comprises either parts of or the complete molecule, but always includes the discontinuous helices. The helix-peptide-helix motif is correlated with the ion translocation function. The extended peptides with their backbone atoms, the helix termini and the polar/charged amino acid residues in close vicinity provide the basis for ion recognition, binding and translocation.     

蚕蛹水解液的氨基酸分组分离法

采用７３２、７１７树脂对蚕蛹酸水解液进行分离。７３２树脂先将蚕蛹水解液粗略分成酸性、中性、碱性氨基酸,７１７树脂再将中性氨基酸分成甘氨酸－丙氨组酸和亮氨酸－异亮氨酸－缬氨酸组。其中亮、异亮、缬氨酸的含量达到７５．９％;同时还进行了脯氨酸的分离,经７１７树脂分离得到的脯氨酸的含量为５０．６％。     

Preparation and characterisation of immobilised metal ion hollow-fibre polysulphone membranes. Their application in high-speed pectic enzyme fractionation

Chelating hollow-fibre membranes were prepared from epoxy-activated polysulphone microfiltration fibres by introducing iminodiacetic acid (IDA) groups in the presence of dimethyl sulphoxide. Fibres with 160, 350 and 620 μmol epoxy groups/ml provided ligand densities of 69, 134 and 203 μmol IDA/ml and pure water fluxes of 7.8, 5.8 and 0.42 cm/min, respectively. However, lysozyme capacity was close to 4 μmol/ml for all fibres. Adsorption isotherms for lysozyme and pectinesterase did not fit Langmuir-type curves and the existence of two types of ligand (A and B) with different accessibility to proteins was assumed. For pectinesterase, maximum capacities of 5100 and 2900 U/ml and dissociation constants of 25 and 316 U/ml were found, respectively, for ligands A and B. For lysozyme, maximum capacities were 2.9 and 0.9 μmol/ml and dissociation constants 5.0 and 102 μM, respectively, for said ligands. A cartridge assembled with IDA hollow fibres had a dynamic capacity for pectinesterase of 7509 U/ml. Productivity of this cartridge for pectic enzyme fractionation was 750 pectinesterase U/ml min, far higher than that obtained with a chelating soft gel (81 pectinesterase U/ml min).     

Identification of the binding interface involved in linkage of cytoskeletal protein 4.1 to the erythrocyte anion exchanger.

Linkages of the cytoskeleton to integral membrane proteins of the plasma membrane have been shown to be important for diverse cellular functions. The erythrocyte membrane provides the best studied example of how the spectrin-actin based membrane cytoskeleton is linked via two proteins, ankyrin and protein 4.1, to the anion exchanger (anion exchanger 1, AE1). Although these and other types of cytoskeleton-membrane connections have been well documented by in vitro binding studies it has not been possible to establish any of such interactions by defining the binding interface at the amino acid level. In the present study we have performed binding studies between protein 4.1 and AE1 using peptides and corresponding idiotypic and anti-idiotypic antibodies to show that arginine-rich clusters of the cytoplasmic domain of AE1 (IRRRY/LRRRY) serve as a major binding site for a motif with opposite charge and identical hydrophobicity present on the membrane-binding domain of protein 4.1 (LEEDY). Both motifs appear to be highly conserved during evolution and may also be involved in other types of cytoskeleton-membrane association, i.e. in binding of protein 4.1 to the glycophorins.     

Functional analysis of amino acids of the Na+/H+ exchanger that are important for proton translocation

The Na⁺/H⁺ exchanger is an integral membrane protein found in the plasma membrane of eukaryotic and prokaryotic cells. In eukaryotes it functions to exchange one proton for a sodium ion. In mammals it removes intracellular protons while in plants and fungal cells the plasma membrane form removes intracellular sodium in exchange for extracellular protons. In this study we used the Na⁺/H⁺ exchanger of Schizosaccharomyces pombe (Sod2) as a model system to study amino acids critical for activity of the protein. Twelve mutant forms of the Na⁺/H⁺ exchanger were examined for their ability to translocate protons as assessed by a cytosensor microphysiometer. Mutation of the amino acid Histidine 367 resulted in defective proton translocation. The acidic residues Asp145, Asp178, Asp266 and Asp267 were important in the proton translocation activity of the Na⁺/H⁺ exchanger. Mutation of amino acids His98, His233 and Asp241 did not significantly impair proton translocation by the Na⁺/H⁺ exchanger. These results confirm that polar amino acids are important in proton flux activity of Na⁺/H⁺ exchangers.     

Hollow-fibre fermenter using ultrafiltration

Summary A novel bioreactor with hollow fibres was developed to facilitate substrate transfer across membrane walls as well as to retain a continuous cell growth in the shell side. Ultrafiltration was induced through membrane by pressurizing feed solution to the inside of a hollow fibre with inlet and outlet pumps. The ultrafiltrate accumulated outside the hollow fibres was recirculated through a reservoir where a part of solution containing cells and substrate was removed to keep the level of reservoir solution constant. Ethanol production by Saccharomyces cerevisiae was carried out to test the feasibility of this reactor. The productivity of this reactor was compared with that of a continuous stirred tank reactor (CSTR).     

Molecular simulation on the interaction of Ethinylestradiol (EE2) with polymer membranes in wastewater purification

Molecular dynamics (MD) simulations are performed to study the adsorption of solute organic molecules (Ethinylestradiol (EE2) and testosterone) with different polymer membranes such as polyether sulfone (PES), polyvinylidene fluoride (PVDF). The equilibrium MD simulations results for the membrane solution interface system show that the interaction of EE2 with PES is specific and strong, whereas the interaction is weak and non-specific for PVDF. The binding free energies, the non-bonded short range interaction energies and mobility are also consistent with the interaction behaviour found in experiments. The adsorption of testosterone onto PES and PVDF is considered as control system. The result shows that binding free energies of PES and PVDF interacting with organic solute are consistent with experimental result in the order as; PES-EE2 > PES-Testosterone > PVDF-EE2 > PVDF-Testosterone. The formation hydrogen bonds and π–π interactions are observed between the EE2 and PES. In addition, adsorption of EE2 onto polyamide 6-12 (PA612) and polystyrene (PS) membranes are predicted. This simulation study provides molecular insights on the experimental observations and helps as a computational methodology to screen the membrane materials for EE2 removal from wastewater.     

The steady-state properties of an ion exchange membrane with mobile sites

A study of the properties of the steady states of a system composed of two solutions separated by an ion exchange membrane having mobile sites is presented. It is assumed that the membrane is impermeable to coions; the solutions contain no more than two species of counterions, both of the same valence; and no flow of bulk solution occurs. Assuming that all ions are completely dissociated, behave ideally, and have constant mobilities throughout the membrane, explicit expressions are derived for the steady states of the electric current, individual fluxes, and concentration profiles as functions of the compositions of the solutions and of the difference of electric potential between them. The derived expressions are compared with those for an ion exchange membrane having fixed sites; and it is found that the expressions of certain quantities, such as the difference of electric potential between the two solutions for zero current or the ratio of the fluxes of the counterions as functions of the external parameters of the system, are the same for both types of membranes. On the other hand, differences in the behavior of the two types of membranes are found from other expressions-for example, the current-voltage relationship. In the mobile site ion exchanger the current asymptotically approaches finite limiting values for high positive and negative voltages while in the fixed site ion exchanger it is the conductance which approaches finite limiting values.     

Quantification of primary amine groups available for subsequent biofunctionalization of polymer surfaces

Biocompatible polymers are commonly functionalized with specific moieties such as amino groups to modify their surface properties and/or to attach bioactive compounds. A reliable method is usually required to characterize amino group surface densities. In this study, aminated polyethylene terephthalate (PET) films were generated via an aminolysis reaction involving either ethylenediamine molecules (EtDA), in order to vary easily the amino group density on PET surfaces, or 25 kDa polyvinylamine (PVAm) as an alternative reagent preventing bulk damages resulting from the aminolysis reaction. Among commonly used dyes for amino group quantification, Orange II and Coomassie Brillant Blue (CBB) were selected to quantify the extent of amine grafting resulting from these derivatization procedures. Rapid and convenient colorimetric assays were compared to surface atomic compositions obtained from X-ray photoelectron spectroscopy (XPS) measurements. Orange II was found to be the most appropriate dye for quantifying primary amine groups in a reliable and specific way. Due to its unique negative charge and low steric hindrance compared to CBB, the Orange II dye was very sensitive and provided reliable quantification over a wide range of amino group surface densities (ca. 5 to at least 200 pmol/mm(2)). In order to further validate the use of the Orange II dye for amino group quantification, a heterobifunctional linker reacting with amino groups was then grafted on modified PET surfaces. Interestingly, the good correlation between the densities of adsorbed Orange II and covalently grafted linkers suggests that the Orange II method is a relevant, reliable, easy, and inexpensive method to predict the amount of amino groups available for subsequent functionalization of polymer surfaces.     

Interfacial thermodynamics of protein adsorption, ion co-adsorption and ion binding in solution. II. Model interpretation of ion exchange in lysozyme chromatography

In this paper we present a model for the ion exchange effects in protein adsorption. The model is applied to chromatography of lysozyme on strong cation exchanger ‘mono S’. The experimental and general thermodynamic aspects have been discussed in Part 1, the preceding paper. The main modelling assumptions are (i) the charge regulation is confined to the small layer of contact between adsorbed protein and exchanger surface, (ii) the contact layer as a whole is electroneutral and (iii) the number of protein acid/base groups and exchanger surface acid groups which participate in the ion exchange is proportional to the area of the contact layer. The model is fitted to the experimental data by adjustment of only two or three parameters. The experimental co-adsorption numbers are very well reproduced. A few conspicuous features emerge: (i) the number of protein acid/base groups and exchanger surface acid groups in the contact layer varies with the medium conditions, such that the number is higher when the interaction between protein and exchanger surface is stronger. (ii) There is indirect evidence for structural alterations in the upper layers of the exchanger surface: the adsorbed protein is probably partly ‘buried’ in the surface.     

Purification of high value proteins from particle containing potato fruit juice via direct capture membrane adsorption chromatography

Potato fruit juice (PFJ) is a by-product from industrial starch production. It still contains several valuable components such as amino acids, minerals and proteins. An economic technology for the isolation and purification of different native potato proteins is the ion exchange chromatography, which can be performed either by classical bed chromatography or by membrane adsorption chromatography (MA-IEX). An already published MA-IEX process for the downstreaming of PFJ is based on the following steps: prefiltration/microfiltration, fractionation with MA-IEX, ultra-/diafiltration and finally drying. In order to further minimize process complexity and costs, new MA-IEX-modules were designed and tested in this research project to facilitate the processing of crude, particle-containing solutions using a tangential flow through the membranes. Modules with fleece polymer spacers and extruded polymer spacers, as well as different spacer channel sizes were tested for their binding capacities and their long-term stability. An optimized setup was found for the technical scale. Modules with extruded polymer spacers channel size 250 μm show the highest binding capacities (anion exchanger approx. 0.34 mg/cm², cation exchanger approx. 0.16 mg/cm²), while the modules with extruded polymer spacers channel size 480 μm show the best long-term stability with 23 passes without intermediary cleaning.     

Hollow fibre modules as membrane reactor in biocatalysis

As shown in the case of the enzymatic cleavage of Penicillin G by Penicillin acylase hollow fibre modules of the type MLW (molecular separation value of 10,000 Dalton) produced for blood dialysis are also suitable as membrane reactor. The enzymes physically bound in the hollow fibre allow a reproducible reaction rate and are characterized by an acceptable stability. The studies indicate an operating stability which makes possible low production costs of amino penicillin acid.     

Partitioning of gonococcal LPS into phenol and water: Different LPS composition of in vivo and in vitro selected variants

Abstract Depending on the culture conditions, Pyrodictium occultum cells revealed two different types of fibers with significant differences in their width in the electron microscope. During growth on elemental sulfur preferentially fibres with a diameter of about 23 nm (type I) were produced. When elemental sulfur was substituted by thiosulfate fibers with a diameter of around 15 nm (type II), were the main appendages. Both types form hollow cylinders consisting of helically arranged sub-units with a wall thickness of 2–3 nm. A triple- layered unit membrane could not be found.     

Tubular membrane bioreactors for biotechnological processes

This article is an overview of bioreactors using tubular membranes such as hollow fibers or ceramic capillaries for cultivation processes. This diverse group of bioreactor is described here in regard to the membrane materials used, operational modes, and configurations. The typical advantages of this kind of system such as environments with low shear stress together with high cell densities and also disadvantages like poor oxygen supply are summed up. As the usage of tubular membrane bioreactors is not restricted to a certain organism, a brief overview of various applications covering nearly all types of cells from prokaryotic to eukaryotic cells is also given here.     

Fish red blood cells: characteristics and physiological role of the membrane ion transporters

Several membrane ion transporters playing a role in gas transport and exchanges, cell volume regulation and intracellular acid-base regulation have been identified in fish red blood cells (RBCs). This short review focuses on Na+/K+ATPase and its role in establishing the ionic gradients across the membrane, on the Cl-/HCO3- exchanger and its key role in respiration and possibly in inducing a chloride conductance, on the Na+/H+ exchanger and the recent advances on its molecular mechanisms of activation and regulation, on the different types of K-Cl cotransports, the different hypotheses and suggested models and their role in cell volume regulation. There is no evidence in the literature for ionic channels in fish RBCs. We present original data obtained with the patch-clamp technique that shows for the first time the existence of a DIDS-sensitive chloride anionic conductance measured in whole cell configuration and the presence of a stretch-activated nonselective cationic channel recorded in cell-attached and excised inside-out configuration. The part played by these ionic conductances is discussed in relation with their possible involvement in volume regulation.     

Structure of polar pili from Pseudomonas aeruginosa strains K and O

The polar pili of Pseudomonas aeruginosa strains K and O are hollow cylinders with 52 Å outer diameter and 12 Å inner diameter. There is a girdle of low electron density (interpreted as due to a local concentration of hydrophobic amino acid side-chains) centred at 31 Å diameter. Similar X-ray diffraction patterns are obtained from oriented fibres of the two types of pili, to a resolution of 7 Å in the equatorial direction and 4 Å in the meridional direction. The two types of pilin protein subunits have a similar molecular weight, and their sequences contain a number of homologous regions. They form a helical array with 4.06 to 4.08 units per turn of a basic helix that has a pitch of 40.8 Å for strain K pili and 41.3 Å for strain O pili at 75% relative humidity. A method is described for distinguishing between very similar diffraction patterns.There is strong intensity at 10 Å near the equator and at 5 Å near the meridian on the diffraction patterns. This intensity distribution is characteristic of α-helical rods running roughly in the direction of the fibre axis. The orientation of these rods was established by the fit between the transform of an α-helical polyalanine model and the strong near-equatorial layer-line.     

Metabolic regulation of the squid nerve Na⁺/Ca²⁺ exchanger: recent kinetic, biochemical and structural developments

The Na?/Ca2? exchangers are structural membrane proteins, essential for the extrusion of Ca2? from most animal cells. Apart from the transport sites, they have several interacting ionic and metabolic sites located at the intracellular loop of the exchanger protein. One of these, the intracellular Ca2? regulatory sites, are essential and must be occupied by Ca2? to allow any type of ion (Na? or Ca2?) translocation. Intracellular protons and Na? are inhibitory by reducing the affinity of the regulatory sites for Ca2?; MgATP stimulates by antagonizing H? and Na?. We have proposed a kinetic scheme to explain all ionic and metabolic regulation of the squid nerve Na?/Ca2? exchanger. This model uniquely accounts for most of the new kinetic data provided here; however, none of the existing models can explain the trans effects of the Ca(i)2?-regulatory sites on external cation transport sites; i.e. all models are incomplete. MgATP up-regulation of the squid Na?/Ca2? exchanger requires a cytosolic protein, which has been recently identified as a member of the lipocalin super family of Lipid Binding Proteins (LBP or FABP) of 132 amino acids (ReP1-NCXSQ, access to GenBank EU981897). This protein was cloned, expressed and purified. To be active, ReP1-NCXSQ must be phosphorylated from MgATP by a kinase present in the plasma membrane. Phosphorylated ReP1-NCXSQ can stimulate the exchanger in the absence of ATP. Experiments with proteoliposomes proved that this up-regulation can take place just with the lipid membrane and the exchanger protein. The structure of ReP1-NCXSQ predicted from the amino acid sequence has been confirmed by X-ray crystal analysis; it has a "barrel" formed by ten beta sheets and two alpha helices, with a lipid coordinated by hydrogen bonds with Arg 126 and Tyr 128.     

Poly(lactic-co-glycolic acid) hollow fibre membranes for use as a tissue engineering scaffold

Mass transfer limitations of scaffolds are currently hindering the development of 3-dimensional, clinically viable, tissue engineered constructs. We have developed a poly(lactide-co-glycolide) (PLGA) hollow fibre membrane scaffold that will provide support for cell culture, allow psuedovascularisation in vitro and provide channels for angiogenesis in vivo. We produced P(DL)LGA flat sheet membranes using 1, 4-dioxane and 1-methyl-2-pyrrolidinone (NMP) as solvents and water as the nonsolvent, and hollow fibre membranes, using NMP and water, by dry/wet- and wet-spinning. The resulting fibres had an outer diameter of 700 micro m and an inner diameter of 250 micro m with 0.2-1.0 micro m pores on the culture surface. It was shown that varying the air gap and temperature when spinning changed the morphology of the fibres. The introduction of a 50 mm air gap caused a dense skin of 5 micro m thick to form, compared to a skin of 0.5 micro m thick without an air gap. Spinning at 40 degrees C produced fibres with a more open central section in the wall that contained more, larger macrovoids compared to fibres spun at 20 degrees C. Culture of the immortalised osteogenic cell line 560pZIPv.neo (pZIP) was carried out on the P(DL)LGA flat sheets in static culture and in a P(DL)LGA hollow fibre bioreactor under counter-current flow conditions. Attachment and proliferation was statistically similar to tissue culture polystyrene on the flat sheets and was also successful in the hollow fibre bioreactor. The P(DL)LGA hollow fibres are a promising scaffold to address the size limitations currently seen in tissue engineered constructs.