Enhancement and regulation of extracellular protein production by Bacillus brevis 47 through manipulation of cell culture conditions

Bacillus brevis 47 was cultivated in 2 liter fermentors in semidefined media containing polypeptone with or without glucose or fructose. Neither sugar was essential for growth or extracellular (S-layer) protein production, and 2.5 to 3.0 g/L protein was accumulated in the medium. When present, glucose was used very slowly, however, fructose was used much more quickly. Dramatic changes in metabolic indicators (dissolved oxygen and pH) were seen when fructose became depleted, and protease was produced, decreasing the amount of protein ultimatelv accumulated in the medium. Using the change in dissolved oxygen as a marker for the time of addition, polypeptone, fructose, or both were used to stimulate protein production. With the addition of polypeptone, on stimulation was achieved, but protease production was suppressed. Addition of fructose did result in a small stimulation of protein production (to 5 g/L) if added once. Further additions resulted in more growth, but no increase in protein production. Various combinations of polypeptone and fructose were also used, with the most effective combination (fructose added early, fructose and polypeptone added later) resulting in an accumulation of 15 g/L protein in the medium. This is comparable to that seen when B. brevis 47 is grown in a complex glucose medium and stimulated with polypeptone addition at 21 hours. These results are discussed with respect to the structure and function of S-layer proteins, as well as the use of this organism for the production of heterologous proteins.     

Mechanism of insulin aggregation and stabilization in agitated aqueous solutions

Undesirable aggregation of aqueous insulin solutions remains a serious obstacle in the development of alternative methods of diabetes therapy. We investigated the fundamental nature of the aggregation mechanism and proposed stabilization strategies based on a mathematical model for the reaction scheme. Insulin aggregation kinetics in the presence of solid-liquid and air-liquid interfaces were monitored using UV spectroscopy and quasielastic light scattering (QELS). Experimental observations were consistent with our model of monomer denaturation at hydrophobic surfaces followed by the formation of stable intermediate species which facilitated subsequent macroaggregation. The model was used to predict qualitative trends in insulin aggregation behavior, to propose stabilization strategies, and to elucidate mechanisms of stabilization. In the absence of additives, insulin solutions aggregated completely (more than 95% of the soluble protein lost) within 24 h; with sugarbased nonionic detergents, no detectable loss occurred for more than 6 weeks. (c) 1992 John Wiley & Sons, Inc.     

Circular dichroism studies on conformational changes in protein molecules upon adsorption on ultrafine polystyrene particles

The conformational changes in well-characterized model proteins [bovine ribonuclease A (RNase A), horseradish peroxidase, sperm-whole myoglobin, human hemoglobin, and bovine serum albumin (BSA)] upon adsorption on ultrafine polystyrene (PS) particles have been studied using circular dichroism (CD) spectroscopy. These proteins were chosen with special attention to molecular flexibility. The ultrafine PS particles were negatively charged and have average diameters of 20 or 30 nm. Utilization of these ultrafine PS particles makes it possible to apply the CD technique to determine the secondary structure of proteins adsorbed on the PS surface. Effects of protein properties and adsorption conditions on the extent of the changes in the secondary structure of protein molecules upon adsorption on ultrafine PS particles were studied. The CD spectrum changes upon adsorption were significant in the "soft" protein molecules (myoglobin, hemoglobin, and BSA), while they were insingnificant in the "rigid" proteins (RNase A and peroxidase). The soft proteins sustained a marked decrease in alpha-helix content upon adsorption. Moreover, the native alpha-helix content, which is given as the percentage of the alpha-helix content in the free proteins, of adsorbed BSA was found to decrease with decreasing pH and increase with increasing adsorbed amount. These observations confirm some well-known hypotheses for the confirmational chages in protein molecules upon adsorption. (c) 1992 John Wiley & Sons, Inc.     

Functional differentiation and primary metabolism of mouse mammary epithelial cells in extended-batch and hollow-fiber culture

Growth, expression of functional differentiation (as characterized by synthesis and secretion of milk proteins), and primary metabolism were studied for a mouse mammary epithelial cell line, COMMA-1D, in extended-batch and hollow-fiber reactor cultures. Batch cultures were performed on Costar polycarbonate membrane inserts, allowing basal and apical exposure to medium. Protein production was induced in both batch and hollow-fiber cultures in hormonesupplemented medium. In batch cultures, high levels of protein production and secretion were maintained for 18 days. Once differentiation was induced, the rate of deinduction was low, even in medium containing epidermal growth factor (EGF) and serum; cells continued to express and secrete proteins for at least 12 days after prolactin and hydrocortisone were removed. Cells in both batch and hollow-fiber cultures were highly glycolytic and exhibited low rates of glutaminolysis. In batch culture on membrane inserts, cells showed polarized metabolism between the apical and basal side, maintaining significant gradients of glucose and lactate. Medium hormonal composition and subsequent differentiation affected both glucose uptake and lactate yield for COMMA-1D in batch culture. (c) 1992 John Wiley & Sons, Inc.     

Effect of matrices on affinity purification of protein C

One of the critical problems in scale-up of affinity chromatography is the mechanical strength of the support matrix against pressure. Because the costs of both the gel matrix and the ligand for the affinity chromatography are very high, the reusability of gel matrices is directly related to the total production cost. In certain cases, where the source material is viscous (e.g., blood plasma), irreversible deformation of gel matrices can readily occur, necessitating severe constraints in the flow rate. Consequently, productivity is low.We have characterized the system parameters and investigated the performance of various matrices that are commercially available. The experimental system used for this study was the immunoaffinity purification of protein C (an anticoagulant protein) from human blood plasma. The support matrices studied were cross-linked agarose, polymethyl acrylic, cellulose, and polyvinyl alcohol polymers. The major system parameters studied were pressure tolerance, coupling efficiency, adsorption efficiency, and batch adsorption/desorption kinetics of protein C to/from the monoclonal antibody (MAb)-Matrix complex. In addition, the apparent equilibrium constant and bandwidth of the product concentration profile in the eluate were characterized by performing pulse tests.A methodology was developed for evaluating the immunoaffinity colum performance for the separation of protein C. By utilizing the experimentally measured parameters, the flow rate limitation for each purification step was computed. Then, the purification performance of the matrices were evaluated in terms of productivity per unit time. Among the matrices tested, cellulose was superior in overall performance for the immunoaffinity purification of protein C using a 10 cm x 10 cm column.     

Purification of recombinant protein A by aqueous two-phase extraction integrated with affinity precipitation

Aqueous two-phase extraction incorporated affinity precipitation was examined as a technique for protein purification. An enteric coating polymer, Eudragit S100, was employed as a ligand carrier. Eudragit was specifically partitioned to the top phase in the aqueous two-phase systems. For application of this method to purification of recombinant protein A using human IgG coupled to Eudragit in an aqueous two-phase system, 80% of protein A added was recovered with 81% purity. The purity was enhanced 26-fold by thid method. The IgG-Eudragit could be used repeatedly for the purification process. This seperation method should be applicable to industrial-scale purification as a new purification procedure combining the advantages and compensating for the disadvantages of the aqueous two-phase method and affinity precipitation method. (c) 1992 John Wiley & Sons, Inc.     

Changes in Electrophoretic Patterns of Oocyte Proteins during Oocyte Maturation in Oryzias latipes

Changes in the two-dimensional SDS-electrophoretic patterns of extracts of maturing denuded oocytes of the medaka ( Oryzias latipes ) were surveyed. In oocytes without follicular constituents several proteins became detectable in the area between the acidic and slightly basic proteins on the two-dimensional electrophoretograms, while a few of the protein spots disappeared during the process of oocyte maturation. The former proteins were detected also in oocytes that were induced to mature in vivo without breakdown of the germinal vesicle. Several proteins newly observed in extracts of post-vitellogenic oocytes during maturation after breakdown of the germinal vesicle were also identified by two-dimensional electrophoresis. Of several proteins that exhibited noticeable changes in maturing oocytes, only one spot incorporated ¹⁴C-labeled amino acid during maturation, suggesting that post-translational modification of many proteins occurred during oocyte maturation.     

Mapping of the calpain proteolysis products of the junctional foot protein of the skeletal muscle triad junction

Summary The Ca²⁺ activated neutral protease calpain II in a concentration-dependent manner sequentially degrades the Junctional foot protein (JFP) of rabbit skeletal muscle triad junctions in either the triad membrane or as the pure protein. This progression is inhibited by calmodulin. Calpain initially cleaves the 565 kDa JFP monomer into peptides of 160 and 410 kDa, which is subsequently cleaved to 70 and 340 kDa. The 340 kDa peptide is finally cleaved to 140 and 200 kDa or its further products. When the JFP was labeled in the triad membrane with the hydrophobic probe 3-(trifuoromethyl) 3-(m) [¹²⁵I]iodophenyl diazirine and then isolated and proteolysed with calpain II, the [¹²⁵I] was traced from the 565 kDa parent to M _r, 410 kDa and then to 340 kDa, implying that these large fragments contain the majority of the transmembrane segments. A 70-kDa frament was also labeled with the hydrophobic probe, although weakly suggesting an additional transmembrane segment in the middle of the molecule. These transmembrane segments have been predicted to be in the C-terminal region of the JFP. Using an ALOM program, we also predict that transmembrane segments may exist in the 70 kDa fragment. The JFP has eight PEDST sequences; this finding together with the calmodulin inhibition of calpain imply that the JFP is a PEDST-type calpain substrate. Calpain usually cleaves such substrates at or near calmodulin binding sites. Assuming such sites for proteolysis, we propose that the fragments of the JFP correspond to the monomer sequence in the following order from the N-terminus: 160, 70, 140 and 200 kDa. For this model, new calmodulin sequences are predicted to exist near 160 and 225 kDa from the N-terminus. When the intact JFP was labeled with azidoATP, label appeared in the 160 and 140 kDa fragments, which according to the above model contain the GXGXXG sequences postulated as ATP binding sites. This transmembrane segment was predicted by the ALOM program. In addition, calpain and calpastatin activities remained associated with triad component organelles throughout their isolation. These findings and the existence of PEDST sequences suggest that the JFP is normally degraded by calpain in vivo and that degradation is regulated by calpastatin and calmodulin