Membrane separation of protein precipitates: unstirred batch studies

The study examines the use of ultrafiltration and microfiltration membranes for concentrating isoelectric soya protein. Experiments with an unstirred batch cell indicate that the flux is limited by the protein which remains in solution after precipitation of the major proportion. The porosityof the precipitate cake formed is shown to be a second important factor. A significant improvement in flux can be obtained by using membranes which permit passage of the soluble protein and by increasing the precipitate particle size. The results are shown to be within the range predicted theoretically by the two limiting cases of a particulate model and a soluble protein model.     

Membrane separation of protein precipitates: Studies with cross flow in hollow fibers

Hollow fiber ultrafiltration and microfiltration membranes are examined for the processing of isoelectric soya protein precipitate suspensions. A model based on the various resistances to permeate flux is used to describe membrane performance. The main resistance to permeate flux is due to the interaction between the active membrane and the soluble and precipitated protein; that is, as compared with resistances due to the active membrane itself or the membrane support structure, or arising from concentrated soluble or precipitated protein layers over the membrane surface. Soluble protein rejection and precipitate mean particle diameter are correlated with observed values of this main resistance.In contract to the ultrafiltration of soluble proteins, the flux rates observed when processing protein precipitate suspensions under a similar range of operating conditions do not approach a limiting value with increased transmembrane pressure. At high protein concentrations, greater flux rates may be achieved for precipitated as compared with soluble proteins. The use of a microfiltration membrane does not give further improvement in flux rate; this may be attributed to problems of pore fouling with precipitate particles.     

Diffusion of carbon dioxide through lipid bilayer membranes. Effects of carbonic anhydrase, bicarbonate, and unstirred layers

Diffusion of (14)C-labeled CO(2) was measured through lipid bilayer membranes composed of egg lecithin and cholesterol (1:1 mol ratio) dissolved in n-decane. The results indicate that CO(2), but not HCO(3-), crosses the membrane and that different steps in the transport process are rate limiting under different conditions. In one series of experiments we studied one-way fluxes between identical solutions at constant pCO(2) but differing [HCO(3-)] and pH. In the absence of carbonic anhydrase (CA) the diffusion of CO(2) through the aqueous unstirred layers is rate limiting because the uncatalyzed hydration-dehydration of CO(2) is too slow to permit the high [HCO(3-)] to facilitate tracer diffusion through the unstirred layers. Addition of CA (ca. 1 mg/ml) to both bathing solutions causes a 10-100-fold stimulation of the CO(2) flux, which is proportional to [HCO(3-)] over the pH range 7-8. In the presence of CA the hydration- dehydration reaction is so fast that CO(2) transport across the entire system is rate limited by diffusion of HCO(3-) through unstirred layers. However, in the presence of CA when the ratio [HCO(3-) + CO(3=)]:[CO(2)] more than 1,000 (pH 9-10) the CO(2) flux reaches a maximum value. Under these conditions the diffusion of CO(2) through the membrane becomes rate limiting, which allows us to estimate a permeability coefficient of the membrane to CO(2) of 0.35 cm s(-1). In a second series of experiments we studied the effects of CA and buffer concentration on the net flux of CO(2). CA stimulates the net CO(2) flux in well buffered, but no in unbuffered, solutions. The buffer provides a proton source on the upstream side of the membrane and proton sink on the downstream side, thus allowing HCO(3-) to facilitate the net transport of CO(2) through the unstirred layers.     

Separation of proteases from yellowfin tuna spleen by ultrafiltration

Separation of protease, trypsin and chymotrypsin from yellowfin tuna spleen extract by ultrafiltration (UF) using regenerated cellulose membranes with molecular weight cut off (MWCO) 30 and 100 kDa was studied. The 100 kDa membrane had a higher transmission of enzymes than that of the 30 kDa membrane. The enzyme transmission varied from 0.01 to 0.18 and from 0.6 to 0.8 for the 30 kDa membrane and 100 kDa membrane, respectively. The protein transmission was about 0.8 for both membranes. Increasing cross-flow rate and transmembrane pressure (TMP) increased permeate flux. The limiting fluxes at cross-flow rate 120, 240 and 360 L/h for the 30 kDa membrane were 17.3, 43.9 and 54.7 L/m2h, respectively and the limiting fluxes at the same flow rate for 100 kDa membrane were 34.1, 51.1 and 68.4 L/m2h, respectively. The separation of these proteases was achieved using the 30 kDa membrane. The purities of proteases were increased more than ten times at TMP 1.5 bar and cross-flow rate 360 L/h by diafiltration using 30 kDa membrane.     

Weak acid permeability through lipid bilayer membranes. Role of chemical reactions in the unstirred layer

The premeabilities of planar lipid bilayer (egg phosphatidylcholine- decane) membranes to butyric and formic acids were measured by tracer and pH electrode techniques. The purposes of the study were (a) to establish criteria for the applicability of each method and (b) to resolve a discrepancy between previously published permeabilities determined using the different techniques. Tracer fluxes of butyric acid were measured at several concentrations and pH's. Under symmetrical conditions the one-way flux of butyric acid(J) is described by 1/J = 1/Pul ([HA] + [A-]) + 1/Pm([HA]), where Pul and Pm are the unstirred layer and membrane permeability coefficients. Pm determined in this manner is 950 x 10(4) cm s-1. Published values for the butyric acid permeability for egg phosphatidylcholine-decane bilayers are 11.5 x 10(-4) (Wolosin and Ginsburg, 1975) and 640 x 10(-4) cm s-1 (Orbach and Finkelstein, 1980). Wolosin and Ginsburg measured net fluxes from a solution of pH = Pka into an unbuffered solution containing a pH electrode. Orbach and Finkelstein measured tracers fluxes under symmetrical conditions at pH 7.4. We reproduced the results of Wolosin and Ginsburg and showed that their apparently low Pm was caused by unstirred layer effects in their poorly buffered solutions. The permeability to formic acid (pKa = 3.75) measured by both tracer and pH electrode techniques was approximately 10(-2) cm s-1. However, if pm greater than Pul, the pH electrode technique cannot be used for measuring the permeabilities of weak acids with pKa's greater than approximately 4.     

A cross-flow reactor with immobilized pectolytic enzymes for juice clarification

Summary A new system for continuous juices clarification is presented. The bioreactor combines microporous plates commercially available and industrial pectinases immobilized on nylon membranes in a cross-flow configuration. The kinetic behaviour of the reactor for different recirculation flow rates has been determined. Fresh apricot juice has been continuously clarified in the bioreactor with excellent results.     

Effects of intermolecular thiol-disulfide interchange reactions on bsa fouling during microfiltration

Several studies have shown that one of the critical factors governing protein fouling of microfiltration membranes is the presence of denaturedand/or aggregated protein in the bulk solutions. Experiments were performed to evaluate the role of intermolecular disulfide interchange reactionson protein aggregation and membrane fouling during stirred cell microfiltration of bovine serum albumin (BSA). The flux decline during BSA filtration was quite dramatic due to the formation of a protein deposit thatfully covered the membrane pores. This flux decline could be completely eliminated by capping the free sulfhydryl group present on the BSA with eithera carboxymethyl or cysteinyl group, demonstrating the critical importance of this free thiol in the intermolecular aggregation reactions and, in turn, protein fouling. BSA aggregation during storage could be reduced by the addition of metal chelators (EDTA and citrate) or dithiothreitol, orby storage at lower pH (7.0) these solutions all had a significantly lower rate of fouling upon subsequent filtration. This behavior is completely consistent with the known chemistry of the thiol-disulfide interchange reaction, demonstrating that an understanding of these intermolecular (aggregation) reactions can provide a rational framework for the analysis and control of protein fouling in these membrane systems. (c) 1994 John Wiley & Sons, Inc.     

Phosphorylation of rabbit and human erythrocyte membranes by soluble adenosine 3':5'-monophosphate-dependent and -independent protein kinases.

Previous reports from this laboratory and others have established that both the rabbit and human erythrocyte membranes contain multiple protein kinase and phosphate acceptor activities. We now report that these membranes also contain phosphoryl acceptor sites for the soluble cyclic AMP-dependent and -independent protein kinases from rabbit erythrocytes. The rabbit erythrocyte membrane, which does not contain a cyclic AMP-dependent protein kinase, has at least four polypeptides (Bands 2.1, 2.3, 4.5, and 4.8) which are phosphorylated in the presence of the soluble cyclic AMP-dependent protein kinases I, IIa, and IIb isolated from rabbit erythrocyte lysates. The resulting phosphoprotein profile is very similar to that obtained for the cyclic AMP-mediated autophosphorylation of human erythrocyte membranes. The activities of the soluble cyclic AMP-dependent protein kinases toward the membranes have been studied at several pH values. Although the substrate specificity of the three kinases is similar, polypeptide 2.3 appears to be phosphorylated to a greater extent by kinase IIa than by I or IIb. This occurs at all pH values studied. Also apparent is that the pH profile for membrane phosphorylation is different from that of histone phosphorylation. The phosphorylation of membrane proteins can also be catalyzed by the soluble erythrocyte casein kinases. These enzymes are not regulated by cyclic nucleotides and can use either ATP or GTP as their phosphoryl donor. Polypeptides 2.1, 2.9, 4.1, 4.5, 4.8, and 5 of both human and rabbit erythrocyte membranes are phosphorylated in the presence of GTP and the casein kinases. This reaction is optimal at pH 7.5. Experiments were performed to determine whether the phosphorylation of the membranes by the soluble and membrane-bound kinases is additive or exclusive. Our results indicate that after maximal autophosphorylation of the erythrocyte membranes, phosphoryl acceptor sites are available to the soluble cyclic AMP-dependent and -independent protein kinases. Furthermore, after maximal phosphorylation of the membranes with one type of soluble kinase, further 32P incorporation can occur as a result of exposure to the other type of soluble kinase.     

Pressure effects in cross-flow microfiltration of suspensions of whole bacterial cells

The effect of Trans-Membrane Pressure (TMP) on permeate flux during cross-flow microfiltration of bacterial cell suspensions in tubular ceramic membranes is studied experimentally. Continuous filtration experiments with suspensions of whole bacterial cells (Mycobacterium M156) show a dramatic permeate flux decline with increasing TMP. During the very early stages of the filtration process, a linear relationship between permeate flux and TMP is observed, suggesting an initial surface sorption of cells on the membrane surface. At longer times, the permeate flux vs. TMP data exhibit a critical pressure beyond which the permeate flux declines with increasing trans-membrane pressure. This is interpreted in terms of the formation of a compressible cake, whose permeability can be described through the Carman-Kozeny equation.     

Computer model of unstirred layer and intracellular pH changes. Determinants of unstirred layer pH

Transmembrane acid–base fluxes affect the intracellular pH and unstirred layer pH around a superfused biological preparation. In this paper the factors influencing the unstirred layer pH and its gradient are studied. An analytical expression of the unstirred layer pH gradient in steady state is derived as a function of simultaneous transmembrane fluxes of (weak) acids and bases with the dehydration reaction of carbonic acid in equilibrium. Also a multicompartment computer model is described consisting of the extracellular bulk compartment, different unstirred layer compartments and the intracellular compartment. With this model also transient changes and the influence of carbonic anhydrase (CA) can be studied. The analytical expression and simulations with the multicompartment model demonstrate that in steady state the unstirred layer pH and its gradient are influenced by the size and type of transmembrane flux of acids and bases, their dissociation constant and diffusion coefficient, the concentration, diffusion coefficient and type of mobile buffers and the activity and location of CA. Similar principles contribute to the amplitude of the unstirred layer pH transients. According to these models an immobile buffer does not influence the steady-state pH, but reduces the amplitude of pH transients especially when these are fast. The unstirred layer pH provides useful information about transmembrane acid–base fluxes. This paper gives more insight how the unstirred layer pH and its transients can be interpreted. Methodological issues are discussed.     

Arabinogalactan protein in the extracellular space of Phaseolus vulgaris hypocotyls

Most hydroxyproline in the soluble fraction (cytosol, extracellular fluid and the contents of ruptured organelles) of homogenized bean hypocotyls originated from arabinogalactan protein. Using a vacuum infiltration-centrifugation technique, we extracted hydroxyproline-containing compounds from the extracellular space, accounting for about 25% of hydroxyproline in the soluble fraction. The bulk of this material was soluble in 5% trichloroacetic acid and could be precipitated with β-Gal-Yariv reagent. Isoelectrofocusing of the extracellular solution showed a major hydroxyproline peak at low pH, and minor peaks at pH 5 and 9, respectively. We conclude that arabinogalactan protein accounts for most of the salt-soluble, extracellular hydroxyproline-containing compounds.     

Formation of an unfolding intermediate state of soluble chloride intracellular channel protein CLIC1 at acidic pH

CLIC proteins function as anion channels when their structures convert from a soluble form to an integral membrane form. While very little is known about the mechanism of the conversion process, channel formation and activity are highly pH-dependent. In this study, the structural properties and conformational stability of CLIC1 were determined as a function of pH in the absence of membranes to improve our understanding of how its conformation changes when the protein encounters the acidic environment at the surface of a membrane. Although the global conformation and size of CLIC1 are not significantly altered by pH in the range of 5.5-8.2, equilibrium unfolding studies reveal that the protein molecule becomes destabilized at low pH, resulting in the formation of a highly populated intermediate with a solvent-exposed hydrophobic surface. Unlike the intermediates formed by many soluble pore-forming proteins for their insertion into membranes, the CLIC1 intermediate is not a molten globule. Acid-induced destabilization and partial unfolding of CLIC1 involve helix alpha1 which is the major structural element of the transmembrane region. We propose that the acidic environment encountered by CLICs at the surface of membranes primes the transmembrane region in the N-domain, thereby lowering the energy barrier for the conversion of soluble CLICs to their membrane-inserted forms.     

Isolation and Characterization of A Temperature Sensitive Protein from dog Colostrum And Milk

A temperature sensitive protein (one of several) that was soluble at 2°C but reversibly precipitated upon warming to room temperature was isolated from dog milk by precipitation with 50% saturated ammonium sulfate, ion exchange chromatography, centrifugation at 30°C and preparative isoelectric focusing in polyacrylamide gel. The molecular weight by sedimentation equilibrium was 13, 400; however, by thin layer gel filtration it appeared to be much larger. Ultracentrifu-gation studies at conditions near those at which the protein precipitated revealed no evidence of aggregation. The protein had a fairly high content of nonpolar amino acids with proline being in the highest amount. The effects of pH, ionic strength, heat and ethanol on the solubility of the protein were studied. A circular dichroism spectrum of the temperature sensitive protein indicated that the protein is quite unordered. An antiserum against the temperature sensitive protein reacted with each of the other temperature sensitive proteins from milk but not with dog serum or saliva.     

Effect of Permeate Drag Force on the Development of a Biofouling Layer in a Pressure-Driven Membrane Separation System

The effect of permeate flux on the development of a biofouling layer on cross-flow separation membranes was studied by using a bench-scale system consisting of two replicate 100-molecular-weight-cutoff tubular ultrafiltration membrane modules, one that allowed flow of permeate and one that did not (control). The system was inoculated with Pseudomonas putida S-12 tagged with a red fluorescent protein and was operated using a laminar flow regimen under sterile conditions with a constant feed of diluted (1:75) Luria-Bertani medium. Biofilm development was studied by using field emission scanning electron microscopy and confocal scanning laser microscopy and was subsequently quantified by image analysis, as well as by determining live counts and by permeate flux monitoring. Biofilm development was highly enhanced in the presence of permeate flow, which resulted in the buildup of complex three-dimensional structures on the membrane. Bacterial transport toward the membrane by permeate drag was found to be a mechanism by which cross-flow filtration contributes to the buildup of a biofouling layer that was more dominant than transport of nutrients. Cellular viability was found to be not essential for transport and adhesion under cross-flow conditions, since the permeate drag overcame the effect of bacterial motility.     

Protein-catalyzed exchange of phosphatidylinositol between rat brain microsomes and myelin.

Exchange of phosphatidylinositol and phosphatidylcholine between microsomal and myelin membranes has been demonstrated. This exchange is reversible and catalyzed by soluble proteins from the brain homogenate precipitated at pH 5.1. The extent of exchange of phosphatidylinositol from microsomal membrane to myelin is dependent upon pH and temperature, with an optimum around pH 7 and at 50 degrees C. Maximum exchange was observed at approximately equal amounts of microsomal, myelin, and supernatant proteins. The extent of the catalyzed exchange increases 4- to 8-fold upon using sonicated or heat-treated myelin as an acceptor membrane. Heating of microsomal membranes results in no change. The extent of catalyzed exchange of phosphatidylcholine is less than that of the phosphatidylinositol. The exchange of other phospholipids and glycolipids between microsomal and myelin membranes cannot be demonstrated. The catalytic activity of the pH 5.1 supernatant proteins in rat brain for the exchange of phosphatidylinositol increases with age after birth and reaches a maximum around 21 days of age analogous to the process of myelination. The pH 5.1 supernatant proteins from quaking and jimpy mutant mice has normal catalytic activity.     

Combined in-fermenter extraction and cross-flow microfiltration for improved inclusion body processing

In this study we demonstrate a new in-fermenter chemical extraction procedure that degrades the cell wall of Escherichia coli and releases inclusion bodies (IBs) into the fermentation medium. We then prove that cross-flow microfiltration can be used to remove 91% of soluble contaminants from the released IBs. The extraction protocol, based on a combination of Triton X-100, EDTA, and intracellular T7 lysozyme, effectively released most of the intracellular soluble content without solubilising the IBs. Cross-flow microfiltration using a 0.2 microm ceramic membrane successfully recovered the granulocyte macrophage-colony stimulating factor (GM-CSF) IBs with removal of 91% of the soluble contaminants and virtually no loss of IBs to the permeate. The filtration efficiency, in terms of both flux and transmission, was significantly enhanced by in-fermenter Benzonase digestion of nucleic acids following chemical extraction. Both the extraction and filtration methods exerted their efficacy directly on a crude fermentation broth, eliminating the need for cell recovery and resuspension in buffer. The processes demonstrated here can all be performed using just a fermenter and a single cross-flow filtration unit, demonstrating a high level of process intensification. Furthermore, there is considerable scope to also use the microfiltration system to subsequently solubilise the IBs, to separate the denatured protein from cell debris, and to refold the protein using diafiltration. In this way refolded protein can potentially be obtained, in a relatively pure state, using only two unit operations.     

Recovery of residual soluble protein by two-step precipitation process with concomitant COD reduction from the yeast-cultivated cheese whey

The present study was conducted to recover the residual soluble protein after cultivation of yeast (K. marxianus) in cheese whey. Cheese whey continuous fermentation with cell recycle system was carried out at 40 °C and pH 3.5. The yeast biomass was separated from the fermented broth by centrifugation and residual soluble protein from fermented whey supernatant was precipitated by heat treatment (at 100 °C, pH 4.5 and 10 min incubation). The maximum soluble protein recovery up to 53 % was achieved at pH 4.5 with 54 % residual COD removal. However, gravity sedimentable precipitates were obtained at pH 3.5 with 47 % protein recovery. Therefore, the reactor (scale up) study was conducted at pH 3.5 with agitation, which resulted in 68 % of residual soluble protein recovery and simultaneously residual COD removal of 62 %. Further precipitation/coagulation of soluble protein was also evaluated using carboxymethylcellulose (CMC) and then two precipitation (thermal followed by CMC precipitation) processes were combined to increase the protein precipitation, which finally reached up to 81 % of total soluble protein recovery from the supernatant. This optimized process could be applied to recover the residual protein left after fermentation of cheese whey without centrifugation.     

Continuous hydrolysis of tallow with immobilized lipase in a microporous membrane

Thermostable lipase from Thermomyces lanuginosus was immobilized in untreated microporous membranes. Melted tallow pumped through the membrane did not wash the enzyme out. From 0.4 to 0.9% of the soluble activity remained after immobilization with half-lives of 1-2 months or more at 50 degrees C. Membranes can be acid/base washed and reloaded with enzyme with no adverse effects. Buffer was required for a long half-life, and recycling the buffer improved the mass transfer of glycerol out of the immobilized lipase reactor. Immobilized activity was unaffected when the pH of the aqueous product changed from 5.5 to 6.5.     

Self-assembly of influenza hemagglutinin: studies of ectodomain aggregation by in situ atomic force microscopy

We have used in situ tapping mode atomic force microscopy (AFM) to study the structural morphology of two fragments of the influenza hemagglutinin protein bound to supported bilayers. The two proteins that we studied are the bromelain-cleaved hemagglutinin (BHA), corresponding to the full ectodomain of the hemagglutinin protein, and FHA2, the 127 amino acid N-terminal fragment of the HA2 subunit of the hemagglutinin protein. While BHA is water soluble at neutral pH and is known to bind to membranes via specific interactions with a viral receptor, FHA2 can only be solubilized in water with an appropriate detergent. Furthermore, FHA2 is known to readily bind to membranes at neutral pH in the absence of a receptor. Our in situ AFM studies demonstrated that, when bound to supported bilayers at neutral pH, both these proteins are self-assembled as single trimeric molecules. In situ acidification resulted in further lateral association of the FHA2 without a large perturbation of the bilayer. In contrast, BHA remained largely unaffected by acidification, except in areas of exposed mica where it is aggregated. Remarkably, these results are consistent with previous observations that FHA2 promotes membrane fusion while BHA only induces liposome leakage at low pH. The results presented here are the first example of in situ imaging of the ectodomain of a viral envelope protein allowing characterization of the real-time self-assembly of a membrane fusion protein.     

Crossflow microfiltration of recombinant Escherichia coli lysates after high pressure homogenization

Crossflow membrane filtration was used to process recombinant Escherichia coli cell lysates containing protein inclusion bodies after high pressure homogenization. The number of passes through the high pressure homogenizer changed the viscosities and average particle sizes of the cell lysates. The different cell lysates were processed with a hollow fiber unit containing microfiltration membranes and a plate and frame unit with either ultrafiltration or microfiltration membranes. There were differences in permeate flux and protein transmission for the various membranes with the best performing membranes giving permeate fluxes greater than 60 L m(-2) h(-1) and protein transmissions greater than 90%. For a given membrane, no differences were observed between the cell lysates following homogenization with one, two, and three passes at 83 MPa. The lack of a difference between the three lysates is due to their similarities with respect to the released macromolecules and the presence of small (<0.1 mum) cell debris. (c) 1997 John Wiley & Sons, Inc. Biotechnol Bioeng 56: 304-310, 1997.