Issues in the culture of the extremely thermophilic methanogen, Methanothermus fervidus

Basic issues in the culture of the extremely thermophilic archaeon, Methanothermus fervidus, have been investigated, including culture medium formulation, substrate yield and product yield coefficient, growth rate and stoichiometry, and H(2) uptake kinetics. The pH optimum for growth of this organism was estimated at 6.9. Growth medium buffered with PIPES instead of bicarbonate supported both increased growth rate and maximum biomass concentration. Substitution of titanium(III) citrate for the reducing agent sodium sulfide improved culture performance as well. However, independent adjustment of iron and nickel concentrations from 11 to 111 muM, respectively, and carbon dioxide partial pressure from 5 to 20 psia did not impact the culture of M. fervidus significantly. An elemental balance approach was utilized to aid in design of a defined medium to support growth to a target maximum biomass concentration of at least 1.0 g dry wt/L. The growth of this organism was limited by H(2) availability in this reformulated culture medium. The maximum growth rate and biomass concentration achieved in anaerobic vials with the defined medium was 0.16 h(-1) and 0.74 g dry wt/L, respectively. This maximum biomass concentration was a 72% improvement over that obtained with a literature-based defined medium. The Monod parameter, K(s), with H(2) as limiting substrate, was estimated at 1.1 +/- 0.4 psia (55 +/- 20 muM in the broth), based on a H(2) consumption study. Representative values for the substrate yield, Y(X/CO(2) ), and product yield coefficient, Y(CH(4)/) (X), were determined experimentally to be 1.78 +/- 0.04 g dry wt/mol CO(2), and 0.52 +/- 0.01 mol CH(4)/g dry wt, respectively. A bench-scale fermentation system suitable for the culture of extremely thermophilic anaerobes was designed and constructed and proved effective for the culture of M. fervidus. (c) 1993 Wiley & Sons, Inc.     

Factors affecting bio-oxidation of sulfide minerals at high concentrations of solids: a review

Bio-oxidation has proved to be a viable process for the oxidative pretreatment of refractory gold-bearing sulfides. Generally, the oxidation rate is maximal at 20% solids for high sulfide content materials [ca. 30% sulfur]. Low grade ores [1% sulfur] have been successfully oxidized at 55% solids, indicating a link between the sulfide grade of the material and the optimal solids concentration for operation. Concentrations of high solids have been reported to lower oxidation rates, increase lag times, and decrease the ultimate extent of oxidation. This review discusses the various factors that have been proposed as causes of these phenomena. The factors include oxygen and carbon dioxide availability, low bacteria-solids ratio; mechanical damage or inhibition of the bacteria, inhibition of bacterial attachment, and the buildup of toxic leach products or other detrimental substances such as some flotation reagents. (c) 1993 John Wiley & Sons, Inc.     

Kinetics of cell growth and heterologous glucoamylase production in recombinant Aspergillus nidulans

In the work, a study of cell growth and the regulation of heterologous glucoamylase synthesis under the control of the positively regulated alcA promoter in a recombinant Aspergillus nidulans is presented. We found that similar growth rates were obtained for both the host and recombinant cells when either glucose or fructose was employed as sole carbon and energy source. Use of the potent inducer cyclopentanone in concentrations greater than 3 mM resulted n maximum glucoamylase concentration and maximum overall specific glucoamylase concentration over 80 h of batch cultivation. However, cyclopentanone concentrations in excess of 3 mM also showed an inhibitory effect on spore germination as well as fungal growth. In contrast, another inducer, threonine, had no negative effect on spore germination even when concentrations of up to 100 mM were used with either glucose or fructose as carbon source. Glucoamylase synthesis in the presence of glucose plus either inducer did not begin until glucose was totally depleted, suggesting strong catabolite repression. Similar results were obtained when fructose was employed, although low levels of glucoamylase were detected before fructose depletion, suggesting partial catabolite repression. The highest enzyme concentration (570 mg/L) and overall specific enzyme concentration (81 mg/g cell) were observed in batch culture when cyclopentanone was the inducer and fructose the primary carbon source. A maximum glucoamylase concentration of 1.1 g/L and an overall specific glucoamylase concentration of 167 mg/g cell were obtained in a bioreactor using cyclopentanone as the inducer and limited-fructose feeding strategy, which nearly doubles the glucoamylase productivity from batch cultures. (c) 1993 John Wiley & Sons, Inc.     

Fed-batch cultivation of recombinant escherichia coli JM103 and production of the fusion protein SPA::EcoRI in a 60-L working volume airlift tower loop reactor

SPA::EcoRI fusion protein was produced by Escherichia coli JM103 carrying the multicopy expression plasmid pMTC48, the multicopy repressor plasmid pRK248, and the multicopy protection plasmid pEcoR4 in a 60-L working volume airlift tower loop reactor on M9 minimal medium with glucose. Cell mass concentration, total cell count, number of colony-forming units, specific growth rate, yield coefficient, and metabolite (acetate, pyruvate, succinate, lactate, ethanol) concentrations were monitored during the growth phase and gene expression. Gene expression was induced by temperature shift or chemically by isopropyl-thiogalactosidase in the airlift tower loop reactor (ALTR) at constant cultivation time and in a small stirred tank reactor at different cultivation times. During induction, the cultivation medium was supplemented with concentrated Luria-Bertani (LB) medium. The intracellular enzyme activity was evaluated as a function of the time after the start of the induction. It was found that the reduction of the glucose concentration and increase of the dissolved oxygen concentration reduced the acetate produced and increased the intracellular enzyme activity. (c) 1993 John Wiley & Sons, Inc.     

Partitioning behavior and enrichment of proteins with reversed micellar extraction: I. forward extraction of proteins from aqueous to reversed micellar phase

Protein extractions using aerosol OT (AOT)-isooctane reverse micelle solutions have been studied to explore the potential for separating and enriching proteins with the reversed micellar extraction. The effects of pH, ionic strength, and different cations of chlorides in a bulk aqueous phase and of AOT concentration in an organic phase on the partitioning of lysozyme and myoglobin and the solubilization of water are presented in detail. The extraction of lysozyme was affected by the concentration of potassium or barium but was almost independent of that of sodium or calcium, whose ionic diameter is smaller than that of potassium and barium. For the extraction of myoglobin, however, the effect of barium concentration was not appreciable. Lysozyme could be enriched into the reversed micellar phase up to 30 times the aqueous feed concentration. (c) 1993 John Wiley & Sons, Inc.     

Measurements of conformational changes during adhesion of lipid and protein (polylysine and S-layer) surfaces

The adhesion forces between various surfaces were measured using the "surface forces apparatus" technique. This technique allows for the thickness of surface layers and the adhesion force between them to be directly measured in controlled vapor or liquid environments. Three types of biological surfaces were prepared by depositing various lipid-protein monolayers (with thicknesses ranging from 1 to 4 nm) on the inert, molecularly smooth mica surface: (i) hydrophobic lipid monolayers; (ii) amphiphilic polyelectrolyte surfaces of adsorbed polylysine; and (iii) deposited bacterial S-layer proteins. The adhesion, swelling, and wetting properties of these surfaces was measured as a function of relative humidity and time. Initial adhesion is due mainly to the van der Waals forces arising from nonpolar (hydrophobic) contacts. Following adhesive contact, significant molecular rearrangements can occur which alter their hydrophobic-hydrophilic balance and increase their adhesion with time. Increased adhesion is generally enhanced by (i) increased relative humidity (or degree of hydration); (ii) increased contact time; and (iii) increased rates of separation. The results are likely to be applicable to the adhesion of many other biosurfaces, and show that the hydrophobicity of a lipid or protein surface is not an intrinsic property of that surface but depends on its environment (e.g., on whether it is in aqueous solution or exposed to the atmosphere), and on the relative humidity of the atmosphere. It also depends on whether the surface is in adhesive contact with another surface and-when considering dynamic (nonequilibrium) conditions-on the time and previous history of its interaction with that surface. (c) 1993 John Wiley & Sons, Inc.     

Nutrient-split feeding strategy for dialysis cultivation of Escherichia coli

Reduction in nutrient loss during dialysis cultivation of Escherichia coli on a glycerol medium was investigated. A dialysis reactor with an inner fermentation and an outer dialysis chamber was used. Aerobic condition was maintained by limiting the glycerol feed rate to an optimum value which was estimated from the oxygen requirements for glycerol oxidation and oxygen transfer capacity of the reactor. High reduction in nutrient loss was achieved by using water as the dialyzing fluid. However, osmotic movement of water from the dialysis to the fermentation chamber was observed, and the final cell concentration was low. With a nutrient-split feeding strategy (feeding glycerol directly to the fermentation chamber and dialyzing with salt solution), glycerol loss was small, there was no osmotic flux of water to the fermentation chamber, and the cell concentration was high. Both glycerol and salt loss could be avoided, and a cell concentration of 170 g/L was obtained when the dialysis process was substituted by addition of XAD adsorbents to the dialysis chamber. Application of this nutrient-split feeding strategy to cell cultivation in a stirred tank reactor, coupled with dialysis in external dialyzer modules, resulted in low cell concentrations. (c) 1993 Wiley & Sons, Inc.     

Continuous, high level production and excretion of a plasmid-encoded protein by Escherichia coli in a two-stage chemostat

The stable continuous overproduction of a plasmidencoded protein, beta-lactamase, for at least 50 days by Escherichia coli K-12, RB791(pKN), with release into the culture medium has been demonstrated in two-stage chemostats. The second-stage culture was continuously induced with 0.1 mM IPTG. Continuous expression of beta-lactamase could not be sustained with this strain in a single-stage chemostat because of cell death and selection for lac(-1) cells. beta-Lactamase production in the second stage was sensitive to the second-stage dilution rate and the distribution of the limiting substrate (i.e., glucose) between the first and second stages. The fraction of viable, excreting cells and the average copy number in the induced culture was measurably higher under those conditions of dilution rate and substrate distribution which yielded high beta-lactamase levels. The best operating conditions found at 20 degrees C were a first-stage dilution rate of 0.12 h(-1), a second-stage dilution rate of 0.03 h(-1), and equal glucose feed supplied to each stage. Enzymatically active beta-lactamase was produced at a level of 25% of total cellular protein with 90% excretion yielding 300 mg beta-lactamase/L that was 50% pure at an OD(600) < 6. (c) 1993 Wiley & Sons, Inc.     

Solid-state nuclear magnetic resonance investigation of solvent dependence of tyrosyl ring motion in an enzyme

Tyrosyl ring motions in alpha-lytic protease were investigated by solid-state deuterium nuclear magnetic resonance (NMR) spectroscopy in lyophilized enzyme powder, in powder suspended in organic solvents, and in aqueous crystals. Ring flipping rates were determined by examining deuterium quadrupole echo line shapes. Of the four Tyr residues in the enzyme, one was flipping at the slow (< or =10(3) s(-1)) and one at the fast (> or =10(7) s(-1)) exchange limit of the line shape experiment in all the environments tested. Flipping rates of the remaining two Tyr residues depended markedly on the solvent, with the lowest flipping rates (< or =10(3) s(-1) for both residues) observed in the enzyme powder, whether dry or suspended in hydrophobic tert-butyl methyl ether. In hydrophilic dioxane and acetonitrile, the mobility of these residues increased to 10(4) and 10(5) s(-1). The latter rate rose further to 10(6) s(-1) in the hydrated hydrophilic solvents and to > or =10(7) s(-1) in aqueous crystals. The deuterium spectrum of native alpha-lytic protease was compared with that of the enzyme whose active center was covalently modified with an inhibitor, which binds next to Tyr-123, constraining its ring. This experiment revealed that water addition to acetonitrile specifically increased the flipping rate of this active center residue. Librational motions ("wobbling"), estimated by their effect on spin-lattice relaxation times, were slowest in the anhydrous solvents, intermediate in the hydrated solvents, and fastest in the aqueous crystals. Thus, alpha-lytic protease is more rigid in organic solvents than in water, as judged by mobility of its tyrosyl residues. Water stripping by hydrophilic solvents did not increase enzyme rigidity, nor were there clear correlations between mobility and either enzymatic activity or solvent dielectric constant.