Performance assessment of two patent strains ofZymomonas mobilis in batch and continuous fermentations

Summary The performance ofZymomonas mobilis strains ATCC 31821 and ATCC 31823 was assessed in batch and continuous culture. In batch culture using a medium containing 250 g/l glucose, identical maximum specific growth rates of 0.16/h were found, though final biomass concentration and growth yield were significantly lower for ATCC 31 823 than for ATCC 31 821. Final ethanol concentrations in this medium were about 110 g/l vor both organisms. In continuous culture at increasing dilution rates using a medium containing 100 g/l glucose, no significant differences were seen between the two strains with respect to the fermentation parameters studied. For ATCC 31 821, maximum rates of glucose uptake (Q_s) and ethanol produktion (Q_p) of 8.7 g glu/g/h and 4.4 g eth/g/h, respectively, were found. Both strains showed a similar performance at a fixed dilution rate of 0.1/h, where maximum ethanol concentrations of about 68 g/l were reached at a feed glucose concentration of about 139 g/l. At this dilution rate the maximum values of Q_s and Q_p were about 5.8 g glu/g/h and 2.8 g eth/g/h, respectively. Test tube experiments showed that growth, measured as optical density, decreased with increasing concentrations of exogenous ethanol with complete inhibition of growth at ethanol concentrations >8% (v/v). As evidenced by the results presented here, we have been unable to practice the invention as described in U.S. Patent 4,403,034 (Rogers and Tribe 1983).Nomenclature D Dilution rate, 1/h - _max maximum specific growth rate, 1/h - S_R Initial substrate concentration, g glucose/1 - S Residual substrate concentration, g glucose/1 - S₀ Effluent substrate concentration, g glucose/1 - X Blomass concentration; g cells/l - OD₆₂₀ Optical density at 620 nm, dimensionless - [P] Product concentration, g ethanol/1 - Y_x/s Growth yield, g cells/g glucose used - Y_p/s Product yield, g ethanol/g glucose used - %, Yield Percentage yield, Y_p/sx100/Y _p ^s/max =Y_p/sx100/0.51 - Q_s Specific rate of glucose uptake, g glucose/g cells/h - Q_p Specific rate of ethanol formation, g ethanol/g cells/h - m_e Maintenance energy coefficient, g glucose/g cells/h - VP Volumetric productivity, g ethanol/l/h - t Fermentation time, h     

Effects of glycose on NADP and NAD glutamate dehydrogenase activities and their relation to ammonium and pH levels in cultures of Bipolaris maydis race T

NADP-glutamate dehydrogenase (NADP-GDH) and NAD-glutamate dehydrogenase (NAD-GDH) activities from Bipolaris maydis race T (ATCC 36180) were determined by measuring the change in absorbance at 340 nm of either reduced NADP or NAD in a reaction mixture of NH₄C1, -ketoglutarate and a cell free extract of the fungus. NADP-GDH activity was high at 48 h, but low at 72 and 96 h when the fungus was incubated on a reciprocal shaker at 28 °C in a mineral salts medium containing 2 g/l glucose and 4 g/l Lasparagine. In contrast, in these cultures NAD-GDH activity was low at 48 h, but high at 72 and 96 h. At 72 and 96 h glucose was not detected in the culture medium. In addition, levels of ammonium and pH increased from 0.0 moles/ml and pH 5.8 at 48 h to 10.6 moles/ml and pH 7.2 at 72 h, and to 23.0 moles/ml and pH 8.4 at 96 h. Fungal mycelia were transferred after 48 h of incubation on media containing 2 g/l glucose and 4 g/l L-asparagine to fresh media containing 0, 2 or 5 g/l glucose with and without 4 g/l L-asparagine. Twenty-four h after transfer to fresh media containing 5 g/l glucose with L-asparagine or 2 or 5 g/l glucose without L-asparagine, NADP-GDH activity was high and NAD-GDH activity was low. Glucose was detected in the culture medium, ammonium was not detected and the pH remained unchanged or decreased. In contrast, 24 h after transfer to fresh media with 0 or 2 g/l glucose with L-asparagine and on media lacking glucose or L-asparagine, NADP-GDH activity was low and NAD-GDH activity was high. Glucose was not detected in the culture medium, ammonium levels were high and the pH increased. Thus, accumulation of ammonium and pH increases accompanying depletion of glucose in a L-asparagine medium could be related to a change in the capacity of B. maydis race T to assimilate and produce ammonium via pathways involving glutamate dehydrogenases.     

Effect of substrate concentration on ethanol production by Zymomonas mobilis on cellulose hydrolysate

Summary A cellulose hydrolysate from Aspen wood, containing mainly glucose, was fermented into ethanol by a thermotolerant strain MSN77 of Zymomonas mobilis. The effect of the hydrolysate concentration on fermentation parameters was investigated. Growth parameters (specific growth rate and biomass yield) were inhibited at high hydrolysate concentrations. Catabolic parameters (specific glucose uptake rate, specific ethanol productivity and ethanol yield) were not affected. These effects could be explained by the increase in medium osmolality. The results are similar to those described for molasses based media. Strain MSN77 could efficiently ferment glucose from Aspen wood up to a concentration of 60 g/l. At higher concentration, growth was inhibited.Nomenclature S glucose concentration (g/l) - X biomass concentration (g/l) - P ethanol concentration (g/l) - C conversion of glucose (%) - t fermentation time (h) - q_S specific glucose uptake rate (g/g.h) - q_p specific ethanol productivity (g/g.h) - YINX/S biomass yield (g/g) - Y_p/S ethanol yield (g/g) - specific growth rate (h^-1)     

Start-up sensitivity to the initial state of a batch bioreactor for a recombinant Escherichia coli in a complex medium

The sensitivities with respect to the initial state of five key variables describing the performance of a batch bioreactor have been computed from an experimentally validated kinetic model. The system has a recombinant Escherichia coli strain containing the plasmid pBR Eco gap, which codes for glyceraldehyde-3-phosphate dehydrogenase (GAPDH) in a complex medium. Since previous studies have shown the start-up sensitivities to be particularly important, the initial 10% of the duration of fermentation was chosen as the time span. The sensitivities of the cell mass, GAPDH and acetate increased with time while those of glucose and yeast extract remained practically constant.Acetate has a crucial role as it functions as both a product and a reactant. With no acetate in the inoculum, the sensitivities of acetate increased an order of magnitude faster than other sensitivities. However, upon addition of acetate through the inoculum, its sensitivities decreased the fastest and stabilised beyond a starting concentration of about 1 g/l whereas other sensitivities stabilised after 5 to 6 g/l of initial acetate. A three-dimensional envelope in the space of acetate concentration-time-relative sensitivity shows a locus of concentrations for minimum time-dependent acetate sensitivity; this may be maintained through fed-batch operation.List of Symbols a A/A₀ - A g/l initial concentration at any time - A ₀ g/l initial acetate concentration - e E/E₀ - E g/l yeast extract concentration at any time - E ₀ g/l initial yeast extract concentration - g G/G₀ - G g/l glucose concentration at any time - G ₀ g/l initial glucose concentration - k _A ^A g/l inhibition constant for acetate-dependent growth during the acetate phase - k _A ^G g/l inhibition constant for acetate-dependent growth during the glucose phase - k _M ^A 1/h rate constant for acetate phase - k _M ^G 1/h rate constant for glucose phase - K _A g/1 affinity constant for acetate - K _G g/1 affinity constant for glucose - m ^A 1/h coefficient of maintenance in acetate - m _m ^A 1/h maximum value of m ^A - m ^G 1/h coefficient of maintenance in glucose - m _m ^G 1/h maximum value of m ^G - n empirical constant - P P/P₀ - P U/ml GAPDH concentration at any time - P ₀ U/ml initial GAPDH concentration - s _c (i,j) sensitivity of y _i to y _j(0) for A ₀=c - t h time - x X/X₀ - X g/l cell mass concentration at any time - X ₀ g/l initial cell mass concentration - y ₁ x - y₂ g - y₃ a - y₄ e - y ₅ p - y _x/A ^A g/g yield coefficient for cell mass per unit mass of acetate during acetate phase - y _x/A ^G g/g yield coefficient for cell mass per unit mass of acetate during glucose phase - y _x/G g/g yield coefficient for cell mass per unit mass of glucose - y _E/x ^A g/g yield coefficient for yeast extract per unit cell mass during acetate phase - y _P/x ^A g/g yield coefficient for yeast extract per unit cell mass during glucose phase - y _P/x ^A U/g yield coefficient for GAPDH per unit cell mass during acetate phase - y _P/x ^G U/g yield coefficient for GAPDH per unit cell mass during glucose phase Greek Letters ₀ proportionality constant for plasmid loss probability - ₁ 1/h maximum rate of plasmid replication - ₂ 1/h saturation constant of the host component of plasmid replication - regulation function (0 or 1) - regulation function (0 or 1) - exponent of growth inhibition term for acetate during the acetate phase - exponent of growth inhibition term for acetate during the glucose phase - ^A 1/h specific growth rate during acetate phase - _m ^A 1/h maximum value of ^A - ^G 1/h specific growth rate during glucose phase - _m ^G 1/h maximum value of ^G - _c (i,j) ratio of sensitivities, s _c (i,j)/s ₀(i,j) - nondimensional time, t _m ^G      

Low Glucose but Not Galactose Enhances Oxidative Mitochondrial Metabolism in C2C12 Myoblasts and Myotubes

Background

Substituting galactose for glucose in cell culture media has been suggested to enhance mitochondrial metabolism in a variety of cell lines. We studied the effects of carbohydrate availability on growth, differentiation and metabolism of C2C12 myoblasts and myotubes.

Methodology/Principal Findings

We measured growth rates, ability to differentiate, citrate synthase and respiratory chain activities and several parameters of mitochondrial respiration in C2C12 cells grown in media with varying carbohydrate availability (5 g/l glucose, 1 g/l glucose, 1 g/l galactose, and no added carbohydrates). C2C12 myoblasts grow more slowly without glucose irrespective of the presence of galactose, which is not consumed by the cells, and they fail to differentiate without glucose in the medium. Cells grown in a no-glucose medium (with or without galactose) have lower maximal respiration and spare respiratory capacity than cells grown in the presence of glucose. However, increasing glucose concentration above physiological levels decreases the achievable maximal respiration. C2C12 myotubes differentiated at a high glucose concentration showed higher dependency on oxidative respiration under basal conditions but had lower maximal and spare respiratory capacity when compared to cells differentiated under low glucose condition. Citrate synthase activity or mitochondrial yield were not significantly affected by changes in the available substrate concentration but a trend towards a higher respiratory chain activity was observed at reduced glucose levels.

Conclusions/Significance

Our results show that using galactose to increase oxidative metabolism may not be applicable to every cell line, and the changes in mitochondrial respiratory parameters associated with treating cells with galactose are mainly due to glucose deprivation. Moderate concentrations of glucose (1 g/l) in a growth medium are optimal for mitochondrial respiration in C2C12 cell line while supraphysiological concentrations of glucose cause mitochondrial dysfunction in C2C12 myoblasts and myotubes.     

Brevibacterium divaricatum: Influence of nutritional conditions on the wall composition and release of uncross-linked peptidoglycan chains into medium

Purified cell walls, originating from penicillin-treated (3 g/ml, 1 h) and-untreated Brevibacterium divaricatum cells grown on complex (CM) and glucose minimal medium with (MM) or without (Ca-free MM) calcium carbonate, were isolated by two procedures. Electron micrographs and chemical analysis revealed no differences between identically isolated walls with respect to the presence or absence of either penicillin or calcium carbonate in the glucose growth medium. On the contrary, the appearance and peptidoglycan content of the walls was greatly dependent on the procedure used for their isolation and the walls isolated from the cells grown on complex medium contained more materials other than peptidoglycan. It was shown that the presence of calcium carbonate in the glucose minimal medium was essential for accumulation of large amounts of peptidoglycan chains into the medium. Penicillin-induced interruption of cell wall synthesis was prerequisite for manifestation of the calcium carbonate stimulating effect.Abbreviations CM complex medium - MM chemically defined minimal medium based on glucose and containing calcium carbonate - Ca-free MM MM modified only by the omission of calcium carbonate - ET-walls Enzyme treated walls - FPR-walls French press-ruptured walls     

Ultra-violet induced mutations to growth factor requirement and penicillin resistance in a blue-green alga

Summary After exposures to UV, two mutant strains of Phormidium mucicola were isolated which are stable and inheritable:1. Strain 5/5 mL-1 is a photoheterotrophic mutant requiring addition of an organic growth factor to the basal medium which appears fulfilled by either casein hydrolysate, glucose, acetate or vitamin mixture and fails to grow heterotrophically.2. mr/p. This strain shows resistance upto 10.24 g/ml of penicillin whereas the parent does not survive beyond a penicillin dose of 0.1 g/ml.     

Ethanol production during D-xylose,L-arabinose,and D-ribose fermentation by Bacteroides polypragmatus

Summary The specific growth rate () during cultivation of Bacteroides polypragmatus in 2.51 batch cultures in 4–5% (w/v) l-arabinose medium was 0.23 h^-1 while that in either d-xylose or d-ribose medium was lower (=0.19 h^-1). Whereas growth on arabinose or xylose occurred after about 6–8 h lag period, growth on ribose commenced after a 30 h lag phase. The maximum substrate utilization rate for arabinose, ribose and xylose in media with an initial substrate concentration of 4–5% (w/v) was 0.77, 0.76, and 0.60 g/l/h respectively. In medium containing a mixture of glucose, arabinose, and xylose, the utilization of all three substrates occurred concurrently. The maximum amount of ethanol produced after 72 h growth in 4–5% (w/v) of arabinose, xylose, and ribose was 9.4, 6.5, and 5.3 g/l, respectively. The matabolic end products (mol/mol substrate) of growth in 4.4% (w/v) xylose medium were 0.73 ethanol, 0.49 acetate, 1.39 CO₂, 1.05 H₂, and 0.09 butyrate.National Research Council of Canada No. 23406     

Effects of pH-variations on the kinetics of growth and energy metabolism in cultured T-lymphoma cells: a microcalorimetric study.

The progression of T-lymphoma cells (CCRF-CEM) growing in suspension has been monitored during long term (12-28 h) batch experiments using microcalorimetry. In parallel with the calorimetric measurements, changes in cell concentration, pH, p(O2) and concentrations of the main energy sources (glucose and glutamine) were determined. The overall metabolic rate per cell (as reflected by the heat production rate per cell, Pcell) and the growth rate decreased with time. These changes could be attributed solely to the decrease in pH of the medium until the total heat production, Q, exceeded 1.2 J per ml (corresponding to an incubation time of 20 h of a batch having an initial cell concentration of 1 x 10(6) cells per ml). The lowering of p(O2) to a level of 0.02 mmol/l or the decrease in concentrations of glucose and glutamine to 7.7 and 1.3 mmol/l, respectively, did not influence Pcell or the growth pattern. No "crowding effect" was observed for the cells in the investigated concentration range (0.6-1.3) x 10(6) cells per ml.     

Growth and butyric acid production by Clostridium populeti

The growth of Clostridium populeti in 2% (w/v) glucose medium containing 0.2% (w/v) yeast extract was optimal with 10 mM NH₄Cl as the nitrogen source. Although the maximum specific growth rate (=0.32 h^-1) with 5 mM NH₄Cl was similar, the biomass yield was about 30% lower than that at the optimum. Either sodium sulphide or cysteine-HCl at an optimum concentration of 0.33 mM and 5.0 mM respectively, could serve as the sole sulphur source for growth. The growth rate was unaffected by initial glucose concentrations of up to 10% (w/v), but in the presence of 15% glucose it declined by about 35%. The molar yield of butyric acid (mol/mol glucose) declined from 0.70 in 1% (w/v) initial glucose medium to 0.39 in 10% glucose medium. In 5.7% initial glucose medium, butyric acid levels of 6.3 g/l were obtained (0.56 mol butyrate/mol glucose) after 72 h of incubation in 2.5 l batch cultures. A decrease of about 50% in the maximum specific growth rate of C. populeti was observed in the presence of an initial concentration of either 1.2 g/l of butyric acid or 18.9 g/l of acetic acid.This paper is issued as NRCC No. 29032     

Influence of culture conditions on the production of heterologous interleukin 1β by Kluyveromyces lactis

Summary Under the control of the repressible PHO5 promoter, the expression of gene encoding interleukin 1 (Il1) was derepressed when the medium was depleted of free inorganic phosphate (Pi). Maximum heterologous protein synthesis was obtained in the presence of 75 mg KH₂PO₄/1 (for 20 g glucose/l). The successful heterologous protein production greatly depends on nutritional culture conditions as Il1 production efficiency was increased by 83% through optimization of the growth medium. Comparison of different phosphate-limited cultivation strategies led to the development of a batch culture procedure with nutrient pulses to delay induced oxido-fermentative glucose metabolism and increase the Il1 production to 135 mg/l.     

Analytical HPLC of the aridicin glycopeptide complex and its application to fermentation development

Summary A gradient analytical HPLC system was developed to assay titers of the three major components of the aridicin (Ardacin) complex produced byKibdelosporangium aridum (SK&F AAD-216). The separation was performed on a Beckman Ultrasphere column using a gradient of acetonitrile (26–43%) in 0.1 M pH 3.2 phosphate buffer with UV detection at 220 nm. The gradient system was necessary to analyze all three major factors within a reasonable recycle time (14 min) without interference by front eluting impurities. The assay was linear from 12 to 200 g/ml (multipleR ²=0.998), with a standard deviation for retention time of 1.4%. A SepPAK isolation scheme was developed to assay samples in complex matrices such as fermentation broths. Using this assay as a monitor, fermentation medium optimization increased the total titers of the three factors from approximately 5 g/ml to over 200 g/ml. The optimal medium contained glucose, beet molasses and methyl oleate. The latter substrate was particularly effective in enhancingproducation 10-fold, presumably by enhancing the supply of acetly-CoA. This is a biosynthetic precursor of both dihydroxyphenylglycine, present in the nucleus, and the acyl side chains present on the amino-glucuronic acids.     

Increase of hybridoma productivity using an original dialysis culture system

Hybridoma cell growth and monoclonal antibody production were investigated with a laboratory-made system in which cells were grown in dialysis tubing (MW cut-off 25 kD). The dialysis system contained 10 ml of cell suspension and was immersed in 200 ml of culture medium which when replaced or was at 4-day intervals. With this system, monoclonal antibody concentrations similar to those observed in ascites (concentrations in the order of one gramme per liter) were obtained. With no medium replacement, the antibody production was 3.3 g/l and the cell productivity 3.2×10^–8 g of IgM produced per cell in one minute. With medium replacement the antibody production was higher, 4.4 g/l but the cell productivity was lower, 1.49×10^–8 g per cell in one minute. Cells cultivated in non-optimized conditions were better producers than cells growing in a good environment.Abbreviations FCS fetal calf serum - Ig immunoglobulin - MAb monoclonal antibody - MW molecular weight - MWCO molecular weight cut off - RM replaced medium - NRM non replaced medium     

Non-aceticlastic methanogenesis from acetate: acetate oxidation by a thermophilic syntrophic coculture

Methanogenesis from acetate by a rod-shaped enrichment culture grown at 60° C was found to require the presence of two organisms rather than a single aceticlastic methanogen. A thermophilic Methanobacterium which grew on H₂/CO₂ or formate was isolated from the enrichment. Lawns of this methanogen were used to co-isolate an acetate oxidizer in roll tubes containing acetate agar. The rod-shaped acetate oxidizer was morphologically distinct from the methanogen and did not show F₄₂₀ autofluorescence. The coculture completely degraded 40 mol/ml acetate, and produced nearly equal quantities of methane, and methanogenesis was coupled with growth. The doubling time for the coculture at 60°C was 30–40 h and the yield was 2.7±0.3 g dry wt/mol CH₄. Studies with ¹⁴C-labelled substrates showed that the methyl group and the carboxyl group of acetate were both converted primarily to CO₂ by the coculture and that CO₂ was concurrently reduced to CH₄. During growth, there was significant isotopic exchange between CO₂ and acetate, especially with thecarboxyl position of acetate. These results support a mechanism for methanogenesis from acetate by the coculture in which acetate was oxidized to CO₂ and H₂ by one organism, while H₂ was subsequently used by a second organism to reduce CO₂ to CH₄. Since the H₂ partial pressure must be maintained below 10^-4 atm by the methanogen for acetate oxidation to be thermodynamically feasible, this is an example of obligate interspecies hydrogen transfer. This mechanism was originally proposed for a single organism by Barker in 1936.     

Effect of selected inhibitors on growth,pigmentation, and aflatoxin production by Aspergillus parasiticus

We have treated a wild type strain of Aspergillus parasiticus with several known aflatoxin inhibitors in hopes of finding specific metabolic blocks in the aflatoxin biosynthetic pathway. In defined medium, benzole acid (2 and 3 mg/ml), cinnamon (1 mg/ml), and sodium acetate (5 mg/ml) were fungitoxic. Benzoic acid (0.5 and 1 mg/ml), chlorox (5 l/ml), and dimethyl sulfoxide (5 l/ml) did not affect dry weight or mycelial pigmentation. Sodium benzoate (1, 2, 4 and 8 mg/ml) added after 2 days growth inhibited aflatoxin production in two defined media. We were unable to confirm previously published reports that an uncharacterized yellow pigment accumulates with benzoate-inhibition of aflatoxin biosynthesis.     

Requirement of heme for growth of Bacteroides fragilis.

Heme or protoporphyrin IX was required for growth of Bacteroides fragilis in a defined medium. The amount of heme necessary for half-maximal growth was 2 to 10 ng/ml (3.8 to 15 pmol/ml) among the Bacteroides species and strains tested. The growth rate, metabolic products from glucose fermentation, and cell yields were affected by the concentration of heme in the medium and by the length of time the culture was incubated. When heme was growth limiting (4 ng/ml), growth rates decreased by 50%, cultures started producing lactic and fumaric acids, and the cell yields declined. The cell yield for B. fragilis (ATCC 25285) at 24 h in medium containing 6.5 microgram of heme per ml was 69 g (dry weight) of cells per mol of glucose compared to 16 g (dry weight) of cells per mol of glucose with 4 ng of heme per ml. B. fragilis was unable to grow in defined medium when a porphyrin precursor, delta-aminolevulenic acid or porphobilinogen, was added in place of heme.     

Relationship of respiratory pathways in soybean cell suspensions to growth of the cells at various glucose concentrations

Green soybean cells (Glycine max L.) were grown in suspension culture on B₅-medium containing various glucose concentrations (2%, 4% or 8% glucose and 2% glucose + 2% or 6% mannitol). Respiratory parameters have been determined in these cells in relation to growth.The length of the growth phase and the amount of dry weight produced increased with higher glucose concentrations. In cells cultured in the presence of 2% glucose, 4% glucose or 2% glucose + 2% mannitol, the activity of the cytochrome pathway (V _cyt )and the capacity of the alternative pathway (V _alt )were not significantly different. Also the contribution of the alternative pathway to total respiration was essentially the same.The glucose content of cells grown in 2% or 4% glucose was roughly equal, which might explain the absence of any effect of the increased glucose concentration on the respiratory parameters.In cells grown in 8% glucose or on 2% glucose + 6% mannitol, both the activity of the cytochrome pathway and the capacity of the alternative pathway were lower. High values of (approaching 1) were found in these cells, meaning that the alternative pathway is nearly fully operative. This is probably caused by the impairment of the cytochrome pathway due to the high osmotic value of the medium.ATP-production per batch per day has been calculated from oxygen uptake data, integrated and compared with cellular dry weight production to give values of 13-15.3 g dry weight produced mole ATP^-1.The described experiments produce no direct evidence for a function of the alternative pathway as energy overflow in soybean cells. The higher alternative pathway activity in the lag phase might be attributed to the great demand for intermediates during this phase.Abbreviations FW Fresh Weight - BHAM Benzhydroxamate     

3-Aminobenzamide,a potent inhibitor of poly (ADP-ribose) polymerase,causes a rapid death of HL-60 cells cultured in serum-free medium

HL-60 cells transferred from serum-supplemented to serum-free culture medium initially bound to culture plate tightly and then released from the plate on increasing the culture time and resumed exponential growth after about 8 h lag. At the initial stage of the culture, the cells became extremely sensitive to 3-aminobenzamide, a potent inhibitor of poly (ADP-ribose) polymerase, and, at 1 mM, 80 to 90% of the cells were lysed within 20 h, whereas the inhibitor was totally ineffective on the cell growth in serum-supplemented medium at the concentration. Non-inhibitory analogs of the inhibitor were ineffective. Assay of poly(ADP-ribose) polymerase activity in permeable cells indicated that a transient activation of the enzyme occurred during the culture in serum-free medium (the maximum activation was observed at 8 h of the culture). The cells conditioned in serum-free medium for 24 h acquired significant resistancy to the inhibitor. A low concentration of fibronectin (5 to 10/ml) and a relatively high concentration of bovine serum albumin (0.5 to 1 mg/ml) effectively blocked the cell attachment to plate and also the 3-aminobenzamide-induced cell lysis. These results suggest that poly(ADP-ribose) polymerase is involved in a process essential for HL-60 cells to adapt to a serumdeprived growth condition.     

Isolation of auxotrophic and antimetabolite-resistant mutants of the hyperthermophilic bacterium Thermotoga neapolitana

Antimetabolite-resistant and auxotrophic mutants of the hyperthermophilic bacterium Thermotoga neapolitana were isolated to provide strains with genetic backgrounds amenable to genetic analyses. Norleucine, azaleucine, 4-nitropyridine-N-oxide, and 3-amino-1, 2, 4-triazole did not affect growth, while 5-fluorouracil (5 g/ml), 5-methyltryptophan (250g/ml), 6-azauracil (100 g/ml), and 4-fluorophenylalanine (30 g/ml) inhibited growth at the indicated minimum inhibitory concentrations. The effect of 5-fluorouracil was analyzed and found to be bacteriostatic. These inhibitors were used to select spontaneously arising resistant mutants. In addition, auxotrophic mutants requiring leucine, tryptophan, adenine, and histidine were isolated following mutagenesis with ethyl methanesulfonate. Six other auxotrophs with undefined growth requirements were also isolated. These strains will be useful for the development of genetic methods for T. neapolitana.