Yeast Cell Homogenate Research Articles

Direct recovery of malate dehydrogenase from highly viscous yeast cell homogenate by a fluidized bed contactor equipped with an agitator

A fluidized bed adsorption system equipped with an agitator was utilized in this study to direct recover malate dehydrogenase enzyme (MDH) from highly turbid yeast cell homogenate. The adsorption and desorption characteristics of STREAMLINE Direct HST, a high-density mixed-mode adsorbent, for the recovery of MDH from the complex cell homogenate were investigated using equilibrium and kinetic studies. The adsorption of MDH was influenced by adsorption pH, ionic strength, feedstock hydrophobicity, and loading of cell homogenate. The elution of MDH from the adsorbent in packed-bed mode was also demonstrated. Subsequently, dynamic binding performance of STREAMLINE Direct HST in stirred fluidized bed adsorption (SFBA) mode was studied using different rotating speeds of agitator, process liquid velocities, and types of cell homogenate. The effect of cell homogenate viscosity on fluidization characteristics was evaluated. MDH was successfully recovered from 100 mL of crude yeast cell homogenate in a single step, recording 80.45% of MDH yield and a purification factor of 73.23. The SFBA process was scaled up using a 50-mm (internal diameter) adsorption column. The scale-up operation showed a similar performance of MDH purification, proving the linear scalability of this adsorption technique. The elution efficiency and purification factor for MDH can be improved to ∼90% and 73–79 folds by using 10 mM NADH/0.1 M NaCl as a specific eluent.

Functional expression of a bacterial α-ketoglutarate dehydrogenase in the cytosol of Saccharomyces cerevisiae

Efficient production of fuels and chemicals by metabolically engineered micro-organisms requires availability of precursor molecules for product pathways. In eukaryotic cell factories, heterologous product pathways are usually expressed in the cytosol, which may limit availability of precursors that are generated in other cellular compartments. In Saccharomyces cerevisiae, synthesis of the precursor molecule succinyl-Coenzyme A is confined to the mitochondrial matrix. To enable cytosolic synthesis of succinyl-CoA, we expressed the structural genes for all three subunits of the Escherichia coli α-ketoglutarate dehydrogenase (αKGDH) complex in S. cerevisiae. The E. coli lipoic-acid scavenging enzyme was co-expressed to enable cytosolic lipoylation of the αKGDH complex, which is required for its enzymatic activity. Size-exclusion chromatography and mass spectrometry indicated that the heterologously expressed αKGDH complex contained all subunits and that its size was the same as in E. coli. Functional expression of the heterologous complex was evident from increased αKGDH activity in the cytosolic fraction of yeast cell homogenates. In vivo cytosolic activity of the αKGDH complex was tested by constructing a reporter strain in which the essential metabolite 5-aminolevulinic acid could only be synthetized from cytosolic, and not mitochondrial, succinyl-CoA. To this end HEM1, which encodes the succinyl-CoA-converting mitochondrial enzyme 5-aminolevulinic acid (ALA) synthase, was deleted and a bacterial ALA synthase was expressed in the cytosol. In the resulting strain, complementation of ALA auxotrophy depended on activation of the αKGDH complex by lipoic acid addition. Functional expression of a bacterial αKGDH complex in yeast represents a vital step towards efficient yeast-based production of compounds such as 1,4-butanediol and 4-aminobutyrate, whose product pathways use succinyl-CoA as a precursor.

Direct recovery of malate dehydrogenase from highly turbid yeast cell homogenate using dye-ligand affinity chromatography in stirred fluidized bed

Dye-ligand affinity chromatography in a stirred fluidized bed has been developed for the rapid recovery of malate dehydrogenase (MDH) from highly turbid baker's yeast cell homogenate in a single step. The most suitable dye, namely Reactive Orange 4, in its optimal immobilized concentration of 8.78 mg/mL was immobilized onto high-density STREAMLINE matrix. To further examine optimal adsorption and elution conditions, the enzyme recovery operation was carried out using unclarified cell homogenates in stirred fluidized bed system. Aiming to develop a non-specific eluent, namely NaCl, to effectively elute the MDH adsorbed, direct recovery of MDH from highly turbid cell homogenate (50% w/v) in a stirred fluidized bed adsorption system was performed. The proposed system successfully achieved a recovery yield of 73.6% and a purification factor of 73.5 in a single step by using 0.6 M NaCl as an eluent at a high liquid velocity of 200 cm/h.

Expression of Cholesterol Hydroxylase/Lyase System Proteins in Yeast S. cerevisiae Cells as a Self-Processing Polyprotein.

2A peptide discovered in Picornaviridae is capable of self-cleavage providing an opportunity to carry out synthesis of several proteins using one transcript. Dissociation in the 2A sequence during translation leads to the individual proteins formation. We constructed cDNA including genes of the bovine cholesterol hydroxylase/lyase (CHL) system proteins-cytochrome P450scc (CYP11A1), adrenodoxin (Adx) and adrenodoxin reductase (AdR), that are fused into a single ORF using FMDV 2A nucleotide sequences. The constructed vectors direct the expression of cDNA encoding polyprotein P450scc-2A-Adx-2A-AdR (CHL-2A) in Escherichia coli and Saccharomyces cerevisiae. The induced bacterial cells exhibit a high level of CHL-2A expression, but polyprotein is not cleaved at the FMDV sites. In yeast S. cerevisiae, the discrete proteins P450scc-2A, Adx-2A and AdR are expressed. Moreover, a significant proportion of AdR and Adx is present in a fusion Adx-2A-AdR. Thus, the first 2A linker provides an efficient cleavage of the polyprotein, while the second 2A linker demonstrates lower efficiency. Cholesterol hydroxylase/lyase activity registered in the recombinant yeast cell homogenate indicates that the catalytically active CHL system is present in these cells. Consequently, for the first time the mammalian system of cytochrome P450 has been successfully reconstructed in yeast cells through expressing the self-processing polyprotein.

Detection of Acyl-CoA Derivatized with Butylamide for in vitro Fatty Acid Desaturase Assay.

Membrane-bound fatty acid desaturases acting on acyl-CoA contribute to the biosynthesis of unsaturated fatty acids, such as arachidonic acid and docosahexaenoic acid in higher organisms. We propose a simplified method for measuring the desaturase activity that combines the in vitro reaction by desaturase-expressing yeast cell homogenate and the detection of acyl-CoA product as butylamide derivatives by gas chromatography. To set up the in vitro reaction, we traced the in vivo activity of rat liver ∆6 fatty acid desaturase (D6d) expressed in the yeast, Saccharomyces cerevisiae, and determined the time taken for the D6d activity to reach its maximum level. The cell homogenate of yeast expressing the maximum D6d activity was made to react in vitro with linoleoyl-CoA to generate the D6d product, γlinolenoyl-CoA. This product was successfully detected as a peak corresponding to γ-linolenoyl butylamide on gas chromatography. This procedure, with low background expression, using non-labeled acyl-CoA as substrate, will contribute toward developing a simple in vitro desaturase assay. It will also help in elucidating the functions of membrane-bound fatty acid desaturases with various substrate specificities and regioselectivities.

Structural and Biochemical Properties of Lipid Particles from the Yeast Saccharomyces cerevisiae

The two most prominent neutral lipids of the yeast Saccharomyces cerevisiae, triacylglycerols (TAG) and steryl esters (SE), are synthesized by the two TAG synthases Dga1p and Lro1p and the two SE synthases Are1p and Are2p. In this study, we made use of a set of triple mutants with only one of these acyltransferases active to elucidate the contribution of each single enzyme to lipid particle (LP)/droplet formation. Depending on the remaining acyltransferases, LP from triple mutants contained only TAG or SE, respectively, with specific patterns of fatty acids and sterols. Biophysical investigations, however, revealed that individual neutral lipids strongly affected the internal structure of LP. SE form several ordered shells below the surface phospholipid monolayer of LP, whereas TAG are more or less randomly packed in the center of the LP. We propose that this structural arrangement of neutral lipids in LP may be important for their physiological role especially with respect to mobilization of TAG and SE reserves.

Direct recovery of alcohol dehydrogenase from unclarified yeast cell homogenate by IDEBAC using an improved scheme for elution

Procion Red HE-7B was directly immobilized onto STREAMLINE matrix to obtain a moderately substituted dye-ligand matrix in which the dye concentration was 6.72 μmol/ml adsorbent. The adsorption characteristics of alcohol dehydrogenase (ADH) onto the sticky dyed adsorbent in the absence and/or presence of yeast cells and cell debris were investigated. The Langmuir-type isotherm model was reasonably used to describe the adsorption behavior. The results showed that the adsorption characteristics and uptake rate for ADH did not change significantly even in the presence of cells and cell debris. Measurements of adsorption breakthrough curves in expanded beds have shown that the maximum dynamic binding capacity appeared to be significantly affected by the aspect ratio. The dynamic binding capacity of the dyed adsorbent was found to be 50.75 U/ml as the aspect ratio was up to 16. Optimal conditions for elution of the adsorbed ADH were determined in small scale packed bed experiments conducted with clarified yeast cell homogenates. The one-step elution was carried out by injecting a pulse of NAD + (15 mM, one settled bed volume) with 0.3 M NaCl as a carrier, resulting in the adsorbed ADH eluting completely from the sticky dyed adsorbent. This case study on the adsorption/desorption characteristics of the sticky dyed adsorbent for ADH showed that this enzyme could be recovered with a purification factor of 4.6 and yield of 89% by immobilized dye-ligand expanded bed affinity chromatography (IDEBAC) in a single step.

Hydrophobic interaction ligand selection and scale-up of an expanded bed separation of an intracellular enzyme from Saccharomyces cerevisiae

A prototype Streamline-Phenyl matrix was evaluated in a hydrophobic interaction mode for the direct recovery of alcohol dehydrogenase (ADH) from yeast cell homogenate. At 5% breakthrough of ADH, a yield of 100% was obtained for a dynamic expanded bed capacity of 240 U(ADH)/ml matrix with a purification factor of 9.2. This compared with a dynamic capacity of 3013 U(ADH)/ml matrix for the packed bed equivalent and a purification factor of 18. In both systems the purification factor was found to increase simultaneously with a decrease in yield as the load of homogenate or breakthrough of ADH was increased. The expanded bed mode of operation conferred considerable robustness with respect to process fouling. No loss in yield was seen over five cycles of repeat loading with an unclarified homogenate. By contrast the packed bed media showed a decrease in yield from 86 to 56% over the same period. Successful scale up of the expanded bed protocol for a 20% breakthrough was demonstrated over a fourfold increase in column diameter. The application of hydrophobic interaction chromatography mediated expanded bed adsorption and its scale-up is discussed in the context of large-scale operations.

Microfiltration of Protein Precipitate from Clarified Yeast Cell Homogenate for the Recovery of a Soluble Product

A crossflow microfiltration unit was used to recover the soluble proteins from a protein precipitate suspension prepared from disrupted yeast. The effects of the process parameters transmembrane pressure (TMP), crossflow velocity, and suspension concentration on the permeate flux and transmission (sieving coefficient) of soluble proteins were determined. Flux increased with increasing crossflow velocity and decreasing concentration, and increased with increasing TMP up to a critical value at which the flux became independent of pressure. Protein transmission also increased with increasing crossflow and decreasing concentration, but had a maximum value at a critical TMP, near the critical value for flux, and declined at higher pressures. A simple analysis based on film theory indicated that the pattern of variation in measured transmission (i.e., permeate protein concentration divided by feed protein concentration) with increasing TMP was due to two competing factors: increasing protein concentration at the membrane surface and decreasing intrinsic transmission (i.e., transmission calculated with respect to the concentration at the membrane surface). Although flux and transmission both increased with decreasing concentration, it was found that an intermediate concentration gave the best rate of soluble protein recovery. Differences were also noted between the transmission of a target enzyme, alcohol dehydrogenase (ADH), and the overall transmission of total soluble protein.

The influence of complex biological feedstock on the fluidization and bed stability in expanded bed adsorption

The stability of expanded bed adsorption systems (EBA) was studied in biomass containing culture broth by residence time distribution (RTD) experiments, using pulse inputs of fluorescent molecules as tracers. Different commercial adsorbents (Streamline DEAE, SP, Phenyl, Chelating, and AC) were tested at various biomass concentrations (2.5–12 %, wet weight) of whole (Saccharomyces cerevisiae) yeast, yeast cell homogenate, and Escherichia coli homogenate. Analyzing the RTD according to the PDE model (PDE: axially dispersed plug-flow exchanging mass with stagnant zones) allowed the calculation of three parameters: the number of transfer units for mass exchange between mobile and stagnant fraction (N), the Peclet number for overall axial dispersion (P), and the mobile fraction of the liquid in axially dispersed plug flow (φ). When fluidization was performed in particle-free buffer the normalized response signal (after perfect input pulse) was symmetric (N:0; P: 50–100; φ: 1), thus, demonstrating the formation of a homogeneous fluidized (expanded) bed. Upon application of suspended biomass the RTD was skewed, depending on the adsorbent used and the type and level of biomass present in the sample. This situation leads to three different characteristic pictures: the well-fluidized system (N: ≥ 7–10; P: ≥ 40; φ: 0.80–0.90), the system exhibiting bottom channeling (N: < 1–2; P: ≥ 40; φ: 0.5–0.7) and, the system where extensive agglomeration develops (N: 4–7; P: 20–40; φ: < 0.5). These results demonstrate that changes in the hydrodynamics of EBA already take place in the presence of moderate concentrations of biomass. Furthermore, those changes can be quantitatively described mainly in terms of the fraction of stagnant zones in the system, which are formed due to the interaction of biomass and adsorbent. The technique described here can be used to evaluate a certain combination of adsorbent and biomass with regard to its suitability for expanded bed adsorption from whole broth. © 1999 John Wiley & Sons, Inc. Biotechol Bioeng 64: 484–496, 1999.

The influence of complex biological feedstock on the fluidization and bed stability in expanded bed adsorption

The stability of expanded bed adsorption systems (EBA) was studied in biomass containing culture broth by residence time distribution (RTD) experiments, using pulse inputs of fluorescent molecules as tracers. Different commercial adsorbents (Streamline DEAE, SP, Phenyl, Chelating, and AC) were tested at various biomass concentrations (2.5-12 %, wet weight) of whole (Saccharomyces cerevisiae) yeast, yeast cell homogenate, and Escherichia coli homogenate. Analyzing the RTD according to the PDE model (PDE: axially dispersed plug-flow exchanging mass with stagnant zones) allowed the calculation of three parameters: the number of transfer units for mass exchange between mobile and stagnant fraction (N), the Peclet number for overall axial dispersion (P), and the mobile fraction of the liquid in axially dispersed plug flow (varphi). When fluidization was performed in particle-free buffer the normalized response signal (after perfect input pulse) was symmetric (N:0; P: 50-100; varphi: 1), thus, demonstrating the formation of a homogeneous fluidized (expanded) bed. Upon application of suspended biomass the RTD was skewed, depending on the adsorbent used and the type and level of biomass present in the sample. This situation leads to three different characteristic pictures: the well-fluidized system (N: >/= 7-10; P: >/= 40; varphi: 0.80-0.90), the system exhibiting bottom channeling (N: < 1-2; P: >/= 40; varphi: 0.5-0.7) and, the system where extensive agglomeration develops (N: 4-7; P: 20-40; varphi: < 0.5). These results demonstrate that changes in the hydrodynamics of EBA already take place in the presence of moderate concentrations of biomass. Furthermore, those changes can be quantitatively described mainly in terms of the fraction of stagnant zones in the system, which are formed due to the interaction of biomass and adsorbent. The technique described here can be used to evaluate a certain combination of adsorbent and biomass with regard to its suitability for expanded bed adsorption from whole broth. Copyright 1999 John Wiley & Sons, Inc. Biotechol Bioeng 64: 484-496, 1999.

Near-infrared spectroscopy for bioprocess monitoring and control.

This article describes the calibration of a spectroscopic scanning instrument for the measurement of selected contaminants in a complex biological process stream. Its use is for the monitoring of a process in which contaminants are to be removed selectively by flocculation from yeast cell homogenate. The main contaminants are cell debris, protein, and RNA. A low-cost instrument has been developed for sensitivity in the region of the NIR spectrum (from 1900 to 2500 nm) where preliminary work found NIR signatures from cell debris, protein, and RNA. Calibration models have been derived using a multivariate method for concentrations of these contaminants, such as would be found after the flocculation process. Two strategies were compared for calibrating the NIR instrument. In one case, samples were prepared by adding materials representative of the contaminants to clarified yeast homogenate so the contaminant levels were well known but outside the range of interest. In the other case, where samples were like those from the process stream after flocculation and floc removal, there was uncertainty of analysis of contaminant level, but the calibration was in the range of interest. Calibration using process stream samples gave results close to those derived from traditional assays. When the calibration models were used to predict the contaminant concentrations in previously unseen samples, the correlation coefficients between measurements and predictions were above 90% in all cases but one. The prediction errors were similar to the errors in the traditional assays.

Luminol luminescence induced by oxidants in antioxidant-deficient yeasts Saccharomyces cerevisiae.

Luminol chemiluminescence induced in the presence of yeast cells and yeast cell homogenates was significantly induced by exogenous oxidants (hydrogen peroxide and menadione). tert-Butyl hydroperoxide did not stimulate chemiluminescence by itself but augmented menadione-induced chemiluminescence. Comparison of yeast strains deficient in catalase, superoxide dismutase or glutathione showed that only glutathione-deficient strains showed elevated chemiluminescence in this system. These results support the idea that more reactive species than hydrogen peroxide and superoxide are critical in the induction of luminol chemiluminescence.

Fatty acid elongation in yeast--biochemical characteristics of the enzyme system and isolation of elongation-defective mutants.

Elongation of long-chain fatty acids was investigated in yeast mutants lacking endogenous de novo fatty acid synthesis. In this background, in vitro fatty acid elongation was dependent strictly on the substrates malonyl-CoA, NADPH and a medium-chain or long-chain acyl-CoA primer of 10 or more carbon atoms. Maximal activity was observed with primers containing 12-14 carbon atoms, while shorter-chain-length acyl-CoA were almost (octanoyl-CoA) or completely (hexanoyl-CoA, acetyl-CoA) inactive. In particular, acetyl-CoA was inactive as a primer and as extender unit. The Michaelis constants for octanoyl-CoA (0.33 mM), decanoyl-CoA (0.83 mM) lauroyl-CoA (0.05 mM), myristoyl-CoA (0.4 mM) and palmitoyl-CoA (0.13 mM) were determined and were comparable for fatty acid synthesis and elongation. In contrast, the affinity of malonyl-CoA was 17-fold lower for elongation (Km = 0.13 mM) than for the fatty acid synthase (FAS) system. With increasing chain length of the primer (> or = 12:0), fatty acid elongation becomes increasingly sensitive to substrate inhibition. Due to the activation of endogenous fatty acids, ATP exhibits a stimulatory effect at suboptimal but not at saturating substrate concentrations. In the yeast cell homogenate, the specific activity of fatty acid elongation is about 10-20-fold lower than that of de novo fatty acid synthesis. The same elongation activity is observed in respiratory competent and in mitochondrially defective cells. The products of in vitro fatty acid elongation are fatty acids of 15-17 or 22-26 carbon atoms, depending on whether tridecanoyl-CoA or stearoyl-CoA is used as a primer. In vitro, the elongation products are converted in part, by alpha-oxidation, to their odd-chain-length lower homologues or are hydrolyzed to fatty acids. In contrast, no odd-chain-length elongation products or very-long-chain fatty acids (VLCFA) shorter than 26:0 are observed in vivo. Hence, VLCFA synthesis exhibits a higher processivity in vivo than in the cell homogenate. In addition, the in vivo process appears to be protected against side reactions such as hydrolysis or alpha-oxidation. Yeast mutants defective in 12:0 or 13:0 elongation were derived from fas-mutant strains according to their failure to grow on 13:0-supplemented media. In vivo, 12:0 elongation was reduced to 0-10% of the normal level, while 16:0 elongation and VLCFA synthesis were unimpaired. It is concluded that yeast contains either two different elongation systems, or that the respective mutation interferes differentially with medium-chain and long-chain fatty acid elongation. The yeast gene affected in the elongation-defective mutants was isolated and, upon sequencing, identified as the known ELO1 sequence. It encodes a putative membrane protein of 32-kDa molecular mass with no obvious similarity to any of the known FAS component enzymes.

Ion exchange purification of G6PDH from unclarified yeast cell homogenates using expanded bed adsorption

The use of expanded beds of STREAMLINE ion exchange adsorbents for the direct extraction of an intracellular enzyme glucose-6-phosphate dehydrogenase (G6PDH) from unclarified yeast cell homogenates has been investigated. It has been demonstrated that such crude feedstocks can be applied to the bed without prior clarification steps. The purification of G6PDH from an unclarified yeast homogenate was chosen as a model system containing the typical features of a direct extraction technique. Optimal conditions for the purification were determined in small scale, packed bed experiments conducted with clarified homogenates. Results from these experiments were used to develop a preparative scale separation of G6PDH in a STREAMLINE 50 EBA apparatus. The use of an on-line rotameter for measuring and controlling the height of the expanded bed when operated in highly turbid feedstocks was demonstrated. STREAMLINE DEAE has been shown to be successful in achieving isolation of G6PDH from an unclarified homogenate with a purification factor of 12 and yield of 98% in a single step process. This ion exchange adsorbent is readily cleaned using simple cleaning-in-place procedures without affecting either adsorption or the bed expansion properties of the adsorbent after many cycles of operation. The ability of combining clarification, capture, and purification in a single step will greatly simplify downstream processing flowsheets and reduce the costs of protein purification. (c) 1996 John Wiley & Sons, Inc.

Ion exchange purification of G6PDH from unclarified yeast cell homogenates using expanded bed adsorption

Ion exchange purification of G6PDH from unclarified yeast cell homogenates using expanded bed adsorption

Development of an expanded bed technique for an affinity purification of G6PDH from unclarified yeast cell homogenates

The use of an expanded bed of STREAMLINE Red H-7B for the purification of the intracellular glycolytic enzyme glucose 6-phosphate dehydrogenase (G6PDH) directly from untreated preparations of disrupted yeast cells has been investigated. Small-scale experiments, carried out in packed beds, have shown that the optimal pH for adsorption is 6.0 and have enabled optimization of elution conditions using a series of eluents. The dynamic capacity of the adsorbent for G6PDH was determined in a small expanded bed to be 28 units/mL. These results were used to develop a preparative scale separation of G6PDH in a STREAMLINE 50 expanded bed column. G6PDH was purified directly from an unclarified yeast homogenate in 99% yield with an average purification factor in the eluted fraction of 103. Cleaning-in-place (CIP) procedures using 0.5 M NaOH and 4M urea in 60% (v/v) ethanol have demonstrated that the adsorbent can be regenerated with no loss of adsorption capacity of alteration of bed expansion characteristics after many cycles of operation.

Chitin synthetase activity is bound to the plasma membrane and to a cytoplasmic particulate fraction in Candida albicans germ tube cells

Subcellular distribution of chitin synthetase has been studied in germ tubes of Candida albicans. Two fractions with synthetase activity were separated from cell homogenates: (i) a mixed membrane fraction where the enzyme, partly in an active form, is associated with the plasma membrane (isopycnic centrifugation of mixed membrane fraction on linear sucrose gradients resolved a unique peak of activity matching with [ 3H]ConA-labelled membranes at a buoyant density of 1.195 g/ml); and (ii) a cytoplasmic fraction containing fully zymogenic enzyme associated with particles whose buoyant density (determined by isopycnic centrifugation on linear sucrose gradients) depended on the cell breakage conditions. The actual cytoplasmic fraction-enzyme may correspond to particles with buoyant density 1.135 g/ml (chitosomes), whereas the enzyme particles with other densities (1.085 and 1.165 g/ml) probably originated during cell disruption, as has been reported previously to occur during the preparation of yeast cell homogenates.

Differential proteolytic sensitivity of yeast fatty acid synthetase subunits α and β contributing to a balanced ratio of both fatty acid synthetase components

The Saccharomyces cerevisiae genes FAS1 and FAS2 encoding the beta and alpha subunit of yeast fatty acid synthetase (FAS), respectively, were individually deleted by one-step gene disruption. Northern blot analysis of RNA from the resulting fas null allele mutants indicated that deletion of FAS2 did not influence the transcription of FAS1, while FAS2 transcription was significantly reduced in the delta fas1 strain. These data suggest an activating role of subunit beta on FAS2 gene expression or, alternatively, a repression of FAS2 by an excess of its own gene product. Compared to the intact alpha 6 beta 6 complex, the individual FAS subunits synthesized in the delta fas1 or delta fas2 strains exhibit a considerably increased sensitivity towards the proteinases present in the yeast cell homogenate. Using yeast mutants specifically defective in the vacuolar proteinases yscA (PRA1/ PEP4 gene product) and/or yscB (PRB1 gene product), it was shown that in vitro, subunit alpha is efficiently degraded by proteinase yscA while for degradation of subunit beta, the combined action of proteinases yscA and yscB is necessary. In vivo, besides the vacuolar proteinases, an additional proteolytic activity specifically affecting free FAS subunit alpha becomes increasingly apparent in cells entering the stationary growth phase. In contrast, under similar conditions uncomplexed FAS subunit beta is stable in strains lacking the vacuolar proteinases yscA and yscB. The reduced FAS subunit levels, at the stationary phase, were independent of the corresponding FAS transcript concentrations. Thus, differential degradation pathways are obviously removing an excess of either FAS subunit, at least under starvation conditions. A combination of both regulation of FAS gene expression and proteolysis of free FAS polypeptides may therefore explain the equimolar amounts of both FAS subunits observed in yeast wild-type cells.

Selective flocculation of nucleic acids, lipids, and colloidal particles from a yeast cell homogenate by polyethyleneimine, and its scale-up

Nucleic acids, lipid, and colloidal particulate material can be selectively flocculated from a yeast cell homogenate by the cationic polymer polyethyleneimine (PEI). Flocculation can occur from a crude homogenate, a homogenate clarified centrifugally, or by the prior use of sodium tetraborate (borax). Flocculation from a homogenate previously clarified by the use of borax is best suited for large-scale operation. The supernatant obtained following centrifugation is effectively free of nucleic acid, lipid, and particulate material with essentially 100% soluble enzyme recovery. Enzyme specific activity increases by approximately 45% compared to a zero PEI control.