Variation in gene copy number and polymorphism of the human salivary amylase isoenzyme system in Caucasians

Summary The polymorphic patterns of human salivary amylase of a large number of individuals of Caucasian origin were determined by using isoelectric focusing and polyacrylamide gel electrophoresis. Nine different salivary amylase protein variants were found; three of them are recorded for the first time and their heredity is shown. Some of the variants are encoded by haplotypes expressing three allozymes. Most variants display low frequencies. Analysis of the relative intensities of variant-specific isozyme bands, combined with segregation analysis, show that extensive quantitative variation is present in the population. The numbers of salivary amylase genes in some families showing quantitative variation at the protein level have been estimated by the polymerase chain reaction. We present evidence that quantitative variations in amylase protein patterns do not always reflect variations in gene copy number but that other mechanisms are also involved.     

Sialic acid in erythrocytes of patients with amaurotic idiocy and Huntington's chorea

Summary Total erythrocyte sialic acid and lipid-extractable sialic acid were estimated in material obtained from 14 normal subjects, and from 8 parents and 1 sibling of patients suffering from late infantile or juvenile forms of amaurotic idiocy, from 1 patient in the terminal phase of the disease and 2 patients with Huntington's chorea. In contrast to a previous report no increase in lipid-sialic acid was found, nor were the total sialic acid values in the pathological material raised. The cause of these different results is still obscure. The possible role of lipid-peroxidation products is discussed.

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Zusammenfassung Der Gehalt der Erythrocyten an gesamter N-Acetyl-Neuraminsäure und an Lipid-extrahierbarer N-Acetyl-Neuraminsäure wurde bestimmt bei 14 Normalpersonen sowie 8 Eltern und einem Geschwister von Patienten, die an der spätinfantilen oder juvenilen Form der amaurotischen Idiotie litten — bei einem Patienten im terminalen Stadium der Krankheit und bei zwei Patienten mit Chorea Huntington. Im Gegensatz zu einem früheren Bericht fand sich keine Erhöhung der Lipid-N-Acetyl-Neuraminsäure, und auch der Gesamtwert war nicht erhöht. Die Ursache dieser Diskrepanz der Ergebnisse ist noch unbekannt. Die mögliche Bedeutung von Lipid-Peroxidationsprodukten wird diskutiert.

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This work has been made possible by a subsidy received from the Organization for Health Research T. N. O., The Hague, Netherlands.     

Heat-labile enterotoxin of Escherichia coli. Characterization of different crystal forms

Heat-labile enterotoxin (LT) was obtained in large quantities (several-gram amounts) and great purity from Escherichia coli C600 carrying the LT-coding multicopy plasmid EWD299. By growing this strain on a medium that allows high cell densities in the early stationary phase, we increased the net LT production per milliliter by a factor of 200, compared to natural porcine enterotoxigenic E. coli. Adsorption and redesorption on Controlled-Pore Glass usually resulted in a 50-100-fold purification of LT in one simple step, which was followed by established purification procedures. LT shows a natural tendency to form large crystals, which, however, are disordered. After numerous trials, conditions were found which virtually eliminated the disorder. Much better crystals were obtained by employing CdCl2 and KF as coprecipitating agents. CdCl2 yielded crystals which did not contain A subunits as judged by electrophoresis of dissolved crystals. Adding KF results in beautifully shaped crystals which diffracted beyond 2 A and are suitable for a high resolution structure determination.     

Quantitative Physiology of Saccharomyces cerevisiae at Near-Zero Specific Growth Rates

Growth at near-zero specific growth rates is a largely unexplored area of yeast physiology. To investigate the physiology of Saccharomyces cerevisiae under these conditions, the effluent removal pipe of anaerobic, glucose-limited chemostat culture (dilution rate, 0.025 h⁻¹) was fitted with a 0.22-μm-pore-size polypropylene filter unit. This setup enabled prolonged cultivation with complete cell retention. After 22 days of cultivation, specific growth rates had decreased below 0.001 h⁻¹ (doubling time of >700 h). Over this period, viability of the retentostat cultures decreased to ca. 80%. The viable biomass concentration in the retentostats could be accurately predicted by a maintenance coefficient of 0.50 mmol of glucose g⁻¹ of biomass h⁻¹ calculated from anaerobic, glucose-limited chemostat cultures grown at dilution rates of 0.025 to 0.20 h⁻¹. This indicated that, in contrast to the situation in several prokaryotes, maintenance energy requirements in S. cerevisiae do not substantially change at near-zero specific growth rates. After 22 days of retentostat cultivation, glucose metabolism was predominantly geared toward alcoholic fermentation to meet maintenance energy requirements. The strict correlation between glycerol production and biomass formation observed at higher specific growth rates was not maintained at the near-zero growth rates reached in the retentostat cultures. In addition to glycerol, the organic acids acetate, d-lactate, and succinate were produced at low rates during prolonged retentostat cultivation. This study identifies robustness and by-product formation as key issues in attempts to uncouple growth and product formation in S. cerevisiae.Laboratory studies on microorganisms are often performed in batch cultures. During the initial phase of batch cultivation, all nutrients are usually present in excess. As a consequence, the initial specific growth rate, μ, of the microorganism in such cultures equals the maximum specific growth rate, μ_max. In natural environments, the specific growth rate of microorganisms is likely to be constrained by the limited availability of one or more growth-limiting nutrients, resulting in specific growth rates far below μ_max (8, 24). In chemostat cultures fed with a medium containing a single growth-limiting nutrient, the dilution rate determines the specific growth rate. Chemostat cultivation therefore offers the possibility to study microbial physiology at carefully controlled, submaximal specific growth rates and to investigate the effect of specific growth rate on cellular physiology (20). Chemostat cultivation of the yeast Saccharomyces cerevisiae has demonstrated strong effects of specific growth rate on biomass composition (26, 51), product formation (5, 37), and cell size (23). Moreover, during energy-limited growth at low specific growth rates, a relatively large fraction of the energy substrate has to be dissimilated for maintenance-related processes such as maintenance of chemi-osmotic gradients and turnover of cellular components (34). Not surprisingly, recent genome-wide studies have shown strong effects of specific growth rate on levels of mRNAs and proteins (9, 14, 38).In chemostat studies on S. cerevisiae, the steady-state specific growth rate is usually between 0.03 h⁻¹ and 0.40 h⁻¹. While this range is relevant for many industrial applications, there are several incentives to study growth of this yeast at even lower specific growth rates. In many natural environments, growth at a μ of 0.03 h⁻¹, corresponding to a doubling time of 23.1 h, probably still represents extremely fast growth. Furthermore, in industrial applications, S. cerevisiae and other microorganisms can be considered as self-replicating catalysts, and, unless biomass is the desired product, growth can be considered as undesirable by-product formation leading to nonproductive substrate consumption. This problem is further augmented when the excess yeast biomass cannot be valorized because it is genetically modified or has been used for the production of compounds that are not compatible with use as, for example, cattle feed. A third incentive for exploring the physiology of S. cerevisiae at near-zero growth rates is related to the increasing interest in this yeast as a systems biology model for human cells (16, 27, 33). At near-zero growth rates, the age of individual yeast cells becomes much higher than can be achieved in conventional batch or chemostat cultures. Studies on extremely slow growth of S. cerevisiae under defined conditions may therefore provide an interesting model for ageing of human cells.Retentostat cultivation, first proposed by Herbert (18), is a modification of chemostat cultivation that has been specifically designed to study microbial physiology at near-zero specific growth rates. In a retentostat, sometimes referred to as recycling fermentor or recyclostat, the growth-limiting energy substrate is fed at a constant rate, and biomass is retained in the fermentor by an internal filter probe connected to the effluent line or by an external filter module. Prolonged retentostat cultivation should, in theory, result in a situation where the specific growth rate becomes zero and where the specific rate of substrate consumption equals the maintenance energy requirement. This situation is fundamentally different from starvation, which involves deterioration of physiological processes, and from resting states typified by spores, which have little or no metabolic activity. Retentostat cultivation has been applied to several bacterial systems including Escherichia coli (11), Paracoccus denitrificans, and Bacillus licheniformis (49) and the autotrophs Nitrosomonas europaea and Nitrobacter winogradskyi (46, 47). These studies demonstrated that the physiology of these prokaryotes at extremely low specific growth rates could not be accurately predicted by a simple extrapolation of results obtained at higher specific growth rates. In particular, near-zero specific growth rates coincided with increased levels of ppGpp (2), which induces the stringent response, a regulatory program that diverts cellular resources from growth to amino acid biosynthesis (10, 21). Furthermore, it was concluded that extremely slow growth led to a reduction of the maintenance energy requirement of prokaryotes. A recent quantitative analysis on cell retention cultures of S. cerevisiae was performed under severely nitrogen-limited growth conditions and used incomplete cell retention (7), which precluded a quantitative comparison with maintenance energy requirements calculated from energy-limited chemostat cultures.The goal of the present study was to quantitatively analyze the physiology of S. cerevisiae at extremely low specific growth rates in glucose-limited retentostat cultures. To this end, an internal filter probe was introduced in the effluent line of standard laboratory chemostat fermentors and used in long-term cultivation runs with complete cell retention. Anaerobic conditions were chosen to facilitate quantification of catabolic fluxes and growth energetics.     

Inhibition of type 2A secretory phospholipase A2 reduces death of cardiomyocytes in acute myocardial infarction

During acute myocardial infarction (AMI), ischemia leads to necrotic areas surrounded by border zones of reversibly damaged cardiomyocytes, showing membrane flip-flop. During reperfusion type IIA secretory phopholipase A₂ (sPLA₂-IIA) induces direct cell-toxicity and facilitates binding of other inflammatory mediators on these cardiomyocytes. Therefore, we hypothesized that the specific sPLA₂-IIA-inhibitor PX-18 would reduce cardiomyocyte death and infarct size in vivo. Wistar rats were treated with PX-18 starting minutes after reperfusion, and at day 1 and 2 post AMI. After 28 days hearts were analyzed. Furthermore, the effect of PX-18 on membrane flip-flop and apoptosis was investigated in vitro. PX-18 significantly inhibited sPLA₂-IIA activity and reduced infarct size (reduction 73 ± 9%, P < 0.05), compared to the vehicle-treated group, without impairing wound healing. In vitro, PX-18 significantly reduced reversible membrane flip-flop and apoptosis in cardiomyocytes. However, no sPLA₂-IIA activity could be detected, suggesting that PX-18 also exerted a protective effect independent of sPLA₂-IIA. In conclusion, PX-18 is a potent therapeutic to reduce infarct size by inhibiting sPLA₂-IIA, and possibly also by inhibiting apoptosis of cardiomyocytes in a sPLA₂-IIA independent manner. A. van Dijk and P. A. J. Krijnen have contributed equally to the study.     

Key Process Conditions for Production of C4 Dicarboxylic Acids in Bioreactor Batch Cultures of an Engineered Saccharomyces cerevisiae Strain

A recent effort to improve malic acid production by Saccharomyces cerevisiae by means of metabolic engineering resulted in a strain that produced up to 59 g liter⁻¹ of malate at a yield of 0.42 mol (mol glucose)⁻¹ in calcium carbonate-buffered shake flask cultures. With shake flasks, process parameters that are important for scaling up this process cannot be controlled independently. In this study, growth and product formation by the engineered strain were studied in bioreactors in order to separately analyze the effects of pH, calcium, and carbon dioxide and oxygen availability. A near-neutral pH, which in shake flasks was achieved by adding CaCO₃, was required for efficient C₄ dicarboxylic acid production. Increased calcium concentrations, a side effect of CaCO₃ dissolution, had a small positive effect on malate formation. Carbon dioxide enrichment of the sparging gas (up to 15% [vol/vol]) improved production of both malate and succinate. At higher concentrations, succinate titers further increased, reaching 0.29 mol (mol glucose)⁻¹, whereas malate formation strongly decreased. Although fully aerobic conditions could be achieved, it was found that moderate oxygen limitation benefitted malate production. In conclusion, malic acid production with the engineered S. cerevisiae strain could be successfully transferred from shake flasks to 1-liter batch bioreactors by simultaneous optimization of four process parameters (pH and concentrations of CO₂, calcium, and O₂). Under optimized conditions, a malate yield of 0.48 ± 0.01 mol (mol glucose)⁻¹ was obtained in bioreactors, a 19% increase over yields in shake flask experiments.In recent years, biologically produced 1,4-dicarboxylic acids (succinate, malate, and fumarate) have attracted great interest as more sustainable replacements for oil-derived commodity chemicals, such as maleic anhydride (50). Malate is currently mainly produced via petrochemical routes for use in food and beverages (18). Development of a biotechnological production process started in the early 1960s with the investigation of the natural malate producer Aspergillus flavus (2). Although process improvements eventually resulted in high product yields and productivities (6), the potential production of aflatoxins (20) prevented the use of this filamentous fungus in industry. Other investigated natural malate-producing fungi (listed in reference 51) produced insufficient malate for industrial use. With the rational design options of metabolic engineering, microorganisms that do not naturally produce large amounts of malic acid may also be considered as production platforms. Wild-type Saccharomyces cerevisiae strains produce little if any malate but would be an interesting starting point for the construction of an efficient malate producer. This yeast has a relatively high tolerance to organic acids and low pH, and due to its role as a model organism in research, a well-developed metabolic engineering toolbox is available. In addition, wild-type S. cerevisiae strains have GRAS (Generally Regarded As Safe) status, so that modified strains are more likely to be allowed in the production of food-grade malic acid.One of the main challenges in the development of an organic acid-producing strain of S. cerevisiae has been the elimination of ethanol formation, which in wild-type strains occurs even under aerobic conditions when glucose concentrations are high (45). Deletion of the pyruvate decarboxylase-encoding genes was found to prevent ethanolic fermentation (17). After evolutionary engineering to remove the growth defects usually associated with pyruvate decarboxylase-negative S. cerevisiae strains, a strain was obtained that produced large amounts of pyruvate, a direct precursor to malate, when grown on glucose (42). Subsequent overexpression of the anaplerotic enzyme pyruvate carboxylase, a cytosolically relocalized malate dehydrogenase and a heterologous malate transporter from Schizosaccharomyces pombe led to a strain that produced significant amounts of malate (51). Cultivation in calcium carbonate (CaCO₃)-buffered shake flasks resulted in malate titers of up to 59 g liter⁻¹ at a yield of 0.42 mol (mol glucose)⁻¹.There are many differences between cultivation in shake flasks and cultivation in (laboratory or industrial) bioreactors. As shake flask cultures lack online pH monitoring and control, there is often significant pH variation over time. The pH is of particular importance. If the yeast can be persuaded to produce organic acids at lower pH values, this reduces the need for active neutralization and thereby reduces by-product formation such as gypsum. However, thermodynamic constraints on acid export, as well as increased stress levels from (undissociated) acid and the low pH, often limit the ability of the microorganisms to produce acids at low pH (32, 43). For this reason, the poorly soluble compound CaCO₃ has traditionally been used to maintain a near-neutral pH in malic acid-producing microbial cultures (6, 29, 51). Adding CaCO₃ also gives increased concentrations of bicarbonate (and thereby CO₂), a substrate for pyruvate carboxylase in the carboxylation of pyruvate (a C₃ carbon molecule) to oxaloacetate (C₄ carbon), as well as calcium. Calcium is known to be involved in cellular signaling pathways (22, 26, 33, 46) and to influence pyruvate carboxylase activity (21, 24). Finally, oxygen transfer rates in shake flasks are often poor compared to those in stirred (laboratory) bioreactors. The formation of significant concentrations (25 g liter⁻¹) of glycerol, a well-known redox sink in S. cerevisiae (41), in shake flask cultures of the engineered malate-producing strain (51) was a strong indication of oxygen limitation.Initial experiments in aerobic, pH-controlled bioreactor cultures of the malate- and succinate-producing Saccharomyces cerevisiae strain RWB525 yielded only low concentrations of these C₄ dicarboxylic acids. The goal of the present study was to identify process parameters that explain the different production levels in shake flask and bioreactor cultures. To this end, we analyzed, both separately and in combination, the impact of culture pH and concentrations of calcium, carbon dioxide, and oxygen on the production of malate and succinate.