Analysis of immobilized cell bioreactors for desulfurization of flue gases and sulfite/sulfate-laden wastewater

Sulfur dioxide (SO₂) is one of the major pollutantsin the atmosphere that cause acid rain. Microbialprocesses for reducing SO₂ to hydrogen sulfide(H₂S) have previously been demonstrated byutilizing mixed cultures of sulfate-reducing bacteria(SRB) with municipal sewage digest as the carbon andenergy source. To maximize the productivity of theSO₂-reducing bioreactor in this study, variousimmobilized cell bioreactors were investigated: a stirredtank with SRB flocs and columnar reactors with cellsimmobilized in either -carrageenan gel matrix orpolymeric porous BIO-SEP^TM beads. Themaximum volumetric productivity for SO₂reduction in the continuous stirred-tank reactor (CSTR)with SRB flocs was 2.1 mmol SO₂/h·l. The-carrageenan gel matrix used for cellimmobilization was not durable at feed sulfiteconcentrations greater than 2000 mg/l or at sulfite feedrate of 1.7 mmol/h·l. A columnar reactor withmixed SRB cells that had been allowed to grow intohighly stable BIO-SEP polymeric beads exhibited thehighest sulfite conversion rates, in the range of16.5 mmol/h·l (with 100% conversion) to20 mmol/h·l (with 95% conversion). In addition toflue gas desulfurization, potential applications of thismicrobial process include the treatment ofsulfate/sulfite-laden wastewater from the pulp and paper,petroleum, mining, and chemical industries.     

Biological decomposition of dichloromethane from a chemical process effluent

The application of specialized microorganisms to treat dichloromethane (DM) containing process effluents was studied. An aerobic fluidized bed reactor with a working volume of 801 filled with sand particles as carriers for the bacteria was used. Oxygen was introduced into the recycle stream by an injector device. DM was monitored semi-continuously. A processor controlled the feed volume according to the DM effluent concentration. Mineralization rates of 12 kg DM/m_bioreactor ³ · d were reached within about three weeks using synthetic wastewater containing 2000 mg/l DM as single carbon compound. DM from process water of a pharmaceutical plant was reduced from about 2000 mg/l in the feed to below 1 mg/l in the effluent at volumetric loading rates of 3 to 4 kg DM/m_bioreactor ³ · d. Degradation of wastewater components like acetone and isopropanol were favoured, thus making the process less attractive for waste streams containing high amounts of DOC other than of DM. DM concentrations of up to 1000 mg/l were tolerated by the immobilized microorganisms and did not influence their DM degradation capacity. The ability to mineralize DM was lost when no DM was fed to the reactor for 10 days.     

The influence of NaCl on the degradation rate of dichloromethane byHyphomicrobium sp.

The degradation of dichloromethane by the pure strainHyphomicrobium GJ21 and by an enrichment culture, isolated from a continuously operating biological trickling filter system, as well as the corresponding growth rates of these organisms were investigated in several batch experiments. By fitting the experimental data to generally accepted theoretical expressions for microbial growth, the maximum growth rates were determined. The effect of NaCl was investigated at salt concentrations varying from 0 to 1000 mM. Furthermore the dichloromethane degradation was investigated separately in experiments in which a high initial biomass concentration was applied. The results show that microbial growth is strongly inhibited by increased NaCl concentrations (50% reduction of _max at 200–250 mM NaCl), while a certain degree of adaptation has taken place within an operational system eliminating dichloromethane. A critical NaCl concentration for growth of 600 mM was found for the microbial culture isolated from an operational trickling filter, while a value of 375 mM was found for the pure cultureHyphomicrobium GJ21. The substrate degradation appears to be much less susceptible to inhibition by NaCl. Even at 800 mM NaCl relatively high substrate degradation rates are still observed, although this process is again dependent on the NaCl concentration. Here the substrate elimination is due to the maintenance requirements of the microorganisms. The inhibition of the dichloromethane elimination was also investigated in a laboratory scale trickling filter. The results of these experiments confirmed those obtained in the batch experiments. At NaCl concentrations exceeding 600 mM a considerable elimination of dichloromethane was still observed for during several months of operation. These observations indicate that the inhibition of microbial growth offers a significant control parameter against excessive biomass growth in biological trickling filters for waste gas treatment.     

Fed-batch culture of hybridoma cells: comparison of optimal control approach and closed loop strategies

Control of fed-batch culture of hybridoma cells was investigated based on two approaches optimal control theory and feedback control. Experiments were conducted for both approaches-with a feed enriched in glutamine. The optimal feed trajectory, a decreasing one, yielded a final monoclonal antibody (MAb) concentration of 170 mg/l, a three-fold increase compared to a typical batch operation.The feedback strategy relied on the on-line estimation of the net specific growth rate of cells from the measurement of the CO₂ production rate with a mass-spectrometer. A PI controller was then used to maintain the growth rate at a desired value by adjusting the dilution rate to the reactor. For the chosen set-point (0.1 d^–1), the final MAb concentration achieved was about 100 mg/1. It was found that there was a delay in the assimilation of the glutamine that should be included in the model to explain the lower MAb production in feedback mode. A higher production can be expected also for a lower set-point in feedback operation.List of Symbols Amm mM ammonia concentration - CPR l/(ld) carbon dioxide production rate - D _t l/d dilution rate - e _t l/d control error - F L/d feed flow rate - Glc mM glucose concentration - Gln mM glutamine concentration - Lac mM lactate concentration - I mg performance index - k _d l/d specific death rate - K _damm l/(mM · d) kinetic parameter for death rate - K _dgln mM kinetic parameter for death rate - K _dlac l/(mM·d) kinetic parameter for death rate - K _c l controller gain - K _glc mM kinetic parameter for growth rate - K _gln mM kinetic parameter for growth rate - K _tr L/(cell·d) transport coefficient - K l/d kinetic parameter for Mab production - m _glc mM/(cell·d) maintenance coefficient - M _Ab mg/l monoclonal antibody concentration - P _t covariance matrix - q _glc l/(l·cell·d) specific CO₂ production rate - q _glc mM/(cell·d) specific glucose uptake rate - q _gln mM/(cell·d) specific glutamine uptake rate - q _Mab mg/(l·cell·d) specific monoclonal antibody production - t _f d final culture time - T d sampling rate - u control input - V l reactor volume - X cell/l total cells concentration - X _v cell/l viable cells concentration - Y yield coefficient Greek mg/cell variable yield coefficient - ₀ mg/(cell·d) growth-associated kinetic parameter - mg/(cell·d) non growth-associated kinetic parameter - _t+1 defined by Eq. (19) - forgetting factor - l/d specific growth rate - _max l/d specific growth rate - _i d controller integral time constant     

Properties of the phosphate and phosphite transport systems of Phytophthora palmivora

Germlings of Phytophthora palmivora possess at least two systems for the uptake of inorganic phosphate (P_i). The first is synthesized on germination in medium containing 50 M P_i and has a K_m of approx. 30 M (V_max=7–9 nmol P_i/h·10⁶ cells). The second is synthesized under conditions of P_i-deprivation and has a higher affinity for P_i (K_m=1–2 M), but a lower V_max (0.5–2 nmol P_i/h·10⁶ cells). The fungicide phosphite likewise enters the germlings via two different transport systems, the synthesis of which also depends on the concentration of P_i in the medium. The K_m of the lower affinity system is 3 mM (V_max=20 nmol phosphite/h·10⁶ cells) and that of the higher affinity system is 0.6 mM (V_max=12 nmol/h·10⁶ cells). P_i and phosphite are competitive inhibitors for each other's transport in both systems. However, whereas mM concentrations of phosphite are necessary to inhibit P_i transport, only M concentrations of P_i are required to inhibit phosphite transport. A third system of uptake for P_i also exists, since when phosphate-deprived cells are presented with mM concentrations of P_i, they transport the anion at a very high rate (around 100 nmol/h·10⁶ cells). High rates of transport of phosphite are also observed when these cells are presented with mM concentrations of this anion.     

Dichloromethane as the sole carbon source forHyphomicrobium sp. strain DM2 under denitrification conditions

Hyphomicrobium sp. strain DM2 was found to grow anaerobically in the presence of nitrate with methanol, formaldehyde, formate or dichloromethane. The estimated growth rate constants with methanol and dichloromethane under denitrification conditions were 0.04 h^–1 and 0.015 h^–1, respectively, which is twofold and fourfold lower than the rates of aerobic growth with these substrates. Slight accumulation of nitrite was observed in all cultures grown anaerobically with nitrate. Dichloromethane dehalogenase, the key enzyme in the utilization of this carbon source, was induced under denitrification conditions to the same specific activity level as under aerobic conditions. In a fed batch culture under denitrification conditionsHyphomicrobium sp. DM2 cumulatively degraded 35 mM dichloromethane within 24 days. This corresponds to a volumetric degradation rate of 5 mg dichloromethane/l·h and demonstrates that denitrificative degradation offers an attractive possibility for the development of anaerobic treatment systems to remove dichloromethane from contaminated groundwater.     

Caecal water and electrolyte absorption and the effects of acetate and glucose, in dehydrated, low-NaCl diet hens

Summary In vivo electrolyte transport and water absorption from the caeca of dehydrated, low-NaCl diet hens are reported. In the absence of luminal glucose or acetate, net electrolyte transport rates and water absorption are small. When physiological concentrations of acetate (40 mM) are included in the perfusate, Na⁺ transport and water absorption increase significantly (P<0.01): 38±7 eqNa⁺/caecum kg·h and 256±33 l H₂O/caecum · kg · h.A similar increase in water absorption occurs with the inclusion of 15 mM glucose in the perfusate (219±30 l H₂O/caecum · kg · h), however both net Na⁺ and Cl^– absorption increase: 28±6 eq Na⁺/caecum · kg · h and 21±5 eq Cl^–/caecum kg · h.These pronounced increases in electrolyte and water absorption are not accompanied by any significant increase in transmural potential difference.The data presented establish caeca as important sites in the recuperation of water and electrolytes in dehydrated, low-NaCl diet hens.Abbreviations ECPD electrochemical potential difference - PD (transmural) potential difference - PEG polyethylene glycol     

Transport of phenylalanine into vacuoles isolated from barley mesophyll protoplasts

The energy-dependent transport of phenylalanine into isolated vacuoles of barley (Hordeum vulgare L.) mesophyll protoplasts has been studied by silicone-layer floatation filtering. The uptake of this aromatic amino acid into the vacuolar compartment is markedly increased by MgATP, showing saturation kinetics; the K _m values were 0.5 mM for MgATP and 1.2 mM for phenylalanine. V _max for phenylalanine transport was estimated to 140 nmol phenylalanine·(mg·Chl)^-1·h^-1. The transport shows a distinct pH optimum at 7.3 and is markedly inhibited by 40 mM nitrate. Azide (1 mM) and vanadate (400 M) had no or little effect on rates of transport while p-fluorophenylalanine seemed to be an effective inhibitor, indicating a possible competition at an amino-acid carrier. Ionophores such as valinomycin, nigericin or gramicidin were strong inhibitors of phenylalanine transport, indicating that this process is coupled to both the transmembrane pH gradient (pH) and the transmembrane potential ().Abbreviations and symbols BSA bovine serum albumin - Chl chlorophyll - Hepes 4-(2-hydroxyethyl)-1-piperazineethanesulfonic acid - pH transmembrane pH gradient - transmembrane potential     

Biodegradation of dichloromethane in waste water using a fluidized bed bioreactor

Summary Biological treatment of a synthetic waste water containing 120 mM dichloromethane (10.2g/l) was carried out under aerobic conditions using dichloromethane-degrading bacteria as an inoculum. The bacteria were adsorbed to support particles and grown in a fluidized bed bioreactor. Charcoal and sand particles were compared as support materials with regard to abrasion, the maximum degradation rate for dichloromethane and the stability of the biological activity in the system.The use of charcoal led to the incorporation of coal dust into the biomass and to an uncontrollable thickness of the biofilm. Therefore the system became unstable and the biological activity decreased. In contrast sand as support material was indifferent to abrasion and allowed biofilm thickness to be controlled. The dichloromethane degrading capacity of the bioreactor increased during the first 30 days. It reached a steady state level of 1.6 g CH₂Cl₂/lxh. Dichloromethane concentration in the effluent was <0.01 mM (<0.85 mg/l) and consequently the degradation efficiency better than 99.99%.     

Lactic acid production by batch fermentation of whey permeate: A mathematical model

Summary The batch fermentation of whey permeate to lactic acid was improved by supplementing the broth with enzyme-hydrolyzed whey protein. A mathematical model based on laboratory results predicts to a 99% confidence limit the kinetics of this fermentation. Cell growth, acid production and protein and sugar use rates are defined in quantifiable terms related to the state of cell metabolism. The model shows that the constants of the Leudeking-Piret model are not true constants, but must vary with the medium composition, and especially the peptide average molecular weight. The kinetic mechanism on which the model is based also is presented.Nomenclature K _i lactic acid inhibition constant (g/l) - K _pr protein saturation constant during cell growth (g/l) - K _pr protein saturation constant during maintenance (g/l) - K _s lactose saturation constant (g/l) - [LA] lactic acid concentration (g/l) - [PR] protein concentration (g/l) - [S] lactose concentration (g/l) - t time (h) - [X] cell mass concentration (g/l) - , fermentation constants of Leudeking and Piret - specific growth rate (l/h) - Y _{g, LA/S} acid yield during cell growth (g acid/g sugar) - Y _{m, LA/S} acid yield during maintenance (g acid/g sugar) - Y _x/pr yield (g cells/g protein) - specific sugar use rate during cell growth (g sugar/h·g cell) - specific sugar use rate during maintenance (g sugar/h·cell)     

Studies on a continuous recycle reactor for a lipase-catalysed processing of ricebran oil

The authors have developed a continuous recycle reactor which efficiently performs emulsion type enzymatic reactions. The reactor column is filled with immobilised lipase and the reactions are effected by pumping the pre-prepared oil-water emulsion through the bottom of the reactor. A part of the product was recycled back and this type of recycling greatly improves the productivity of fatty acid compared to continuous once-through reactor without recycling. The recycle reactor could be continuously run for 35 days without decrease in conversions. The performance of the reactor was interpreted by a model and the theoretical conversion was compared with the experimental data.List of Symbols F _AO mol/min feed rate - K _M g/l Michaelis constant - R recycle ratio - r ₅ mol/(ml · min) reaction rate - S ₀ g/l initial substrate concentration - V _max mol/(ml · min) maximum reaction velocity - V _R l void volume of the reactor - x _s fractional conversion - Standard deviation      

Sodium influx in isolated gills of the freshwater mussel,Ligumia subrostrata

Summary Isolated gills of the freshwater mussel,Ligumia subrostrata, accumulate Na from a pondwater bathing medium. The rate of Na transport by the isolated gill is 13.2±1.1 mol (g dry gill·10 min)^–1 which equals or exceeds the estimated Na transport rate of intact animals. Sodium influx is saturable with aV _max of 13.6±1.2 mol (g dry gill·10 min)^–1 and an affinity (K _s) of 0.17 mM Na/l. The isolated gills survive prolonged exposure to pondwater with a constant of 890 l O₂ (g dry gill·h)^–1 over a 4 h period. Sodium transport in the isolated gills is stimulated 80% above control values by 10^–4 M serotonin, 60% by 0.5 mM cAMP and 60% by 12.5 g/ml nystatin. Sodium influx is inhibited by 0.5 mM amiloride and 1 mM lithium.     

Anaerobic dechlorination of trichloroethene,tetrachloroethene and 1,2-dichloroethane by an acetogenic mixed culture in a fixed-bed reactor

An anaerobic enrichment culture with glucose as the sole source of carbon and energy plus trichloroethene (TCE) as a potential electron acceptor was inoculated with material from a full size anaerobic charcoal reactor that biologically eliminated dichloromethane from contaminated groundwater (Stromeyer et al. 1991). In subcultures of this enrichment complete sequential transformation of 10 µM TCE viacis-dichloroethene and chloroethene to ethene was reproducibly observed. Maintenance of this activity on subcultivation required the presence of TCE in the medium. The enrichment culture was used to inoculate an anaerobic fixed-bed reactor containing sintered glass Raschig elements as support material. The reactor had a total volume of 1780 ml and was operated at 20 °C in an up-flow mode with a flow rate of 50 ml/h. It was fed continuously with 2 mM glucose and 55 µM TCE. Glucose was converted to acetate as the major product and to a minor amount of methane; TCE was quantitatively dehalogenated to ethene. When, in addition to TCE, tetrachloroethene or 1,2-dichloroethane were added to the system, these compounds were also dehalogenated to ethene. In contrast, 1,1,1-trichloroethane was not dehalogenated, but at 40 µM severely inhibited acetogenesis and methanogenesis. When the concentration of TCE in the feed was raised to 220 µM, chloroethene transiently accumulated, but after an adaptation period ethene was again the only volatile product detected in the effluent. The volumetric degradation rate at this stage amounted to 6.2 µmol/l/h. Since complete transformation of TCE occurred in the first sixth of the reactor volume, the degradation capacity of the system is estimated to exceed this value by factor of about ten.Abbreviations CA chloroethane - 1,1-DCA 1,1-dichloroethane - 1,2-DCA 1,2-dichloroethane - 1,1-DCE 1,1-dichloroethene - c-DCE cis-1,2-dichloroethene - t-DCE trans-1,2-dichloroethene - PCE tetrachloroethene, perchloroethene - 1,1,1-TCA 1,1,1-trichloroethane - TCE trichloroethene - VC chloroethene, vinyl chloride     

Anaerobic acetate oxidation to CO2 by Desulfotomaculum acetoxidans

Desulfotomaculum acetoxidans has been proposed to oxidize acetate to CO₂ via an oxidative acetyl-CoA/carbon monoxide dehydrogenase pathway rather than via the citric acid cycle. We report here the presence of the enzyme activities required for the operation of the novel pathway. In cell extracts the following activities were found (values in brackets=specific activities and apparent K _m; 1 U·mg^-1=1 mol·min^-1·mg protein^-1 at 37°C): Acetate kinase (6.3 U·mg^-1; 2 mM acetate; 2.4 mM ATP); phosphate acetyltransferase (60 U·mg^-1, 0.4 mM acetylphosphate; 0.1 mM CoA); carbon monoxide dehydrogenase (29 U·mg^-1; 13% carbon monoxide; 1.3 mM methyl viologen); 5,10-methylenetetrahydrofolate reductase (3 U·mg^-1, 0.06 mM CH₃–FH₄); methylenetetrahydrofolate dehydrogenase (3.6 U·mg^-1, 0.9 mM NAD, 0.1 mM CH₂=FH₄); methenyltetrahydrofolate cyclohydrolase (0.3 U·mg^-1); formyltetrahydrofolate synthetase (3 U·mg^-1, 1.4 mM FH₄, 0.4 mM ATP, 13 mM formate); and formate dehydrogenase (10 U·mg^-1, 0.4 mM formate, 0.5 mM NAD). The specific activities are sufficient to account for the in vivo acetate oxidation rate of 0.26 U·mg^-1.Non-standard abbreviations FH₄ Tetrahydrofolate - CHO-FH₄ N¹⁰-formyltetrahydrofolate - CHFH₄ N⁵,N¹⁰-methenyltetrahydrofolate - CH₂=FH₄ N⁵,N¹⁰-methylenetetrahydrofolate - CH₃–FH₄ N⁵-methyltetrahydrofolate - MOPS morpholinopropane sulfonic acid - DTT d,l-1,4-dithiothreitol - TRIS tris-(hydroxymethyl)-aminomethane - Ap₅A p¹,P⁵-di(adenosine-5)pentaphosphate - MV methyl viologen     

Effects of hypoxia on lipolysis in isolated rat myocardial cells

Summary The effect of hypoxia on myocardial lipolysis (glycerol release) was investigated in freshly isolated, calcium-tolerant rat ventricular myocytes. Hypoxia was produced by gassing the incubation medium (Joklik-minimum essential medium, supplemented with 1.2 mM MgSO₄, 1 mM DL-carnitine, 1.5 mM CaCl₂ and 0.6 mM palmitate bound to 0.15 mM fatty acid free bovine serum albumin) with 95% N₂–5% CO,. Control (normoxic) incubations were carried out under air-5% CO₂ atmosphere. Basal glycerol release increased from 46.6 ± 3.0 nmol/106 cells · 30 min in normoxia to 64.5 ± 4.3 nmol/10⁶ cells · 30 min in hypoxia (p < 0.05). Addition of isoprenaline (10 M) resulted in a significant (p < 0.05) stimulation of the glycerol release both in normoxia and in hypoxia, but the enhancement above basal rates was apparently lower in hypoxia (8.7 ± 2.5 nmol/10⁶ cells · 30 min) than in normoxia (12.2 ± 2.7 nmol/106 cells · 30 min). Furthermore, whereas the isoprenaline-induced rise in lipolysis both in normoxia and hypoxia was prevented by inclusion of propranolol (10 M), propranolol did not affect the hypoxia-induced increase in lipolysis. Thus, the above findings suggest that myocardial lipolysis may be stimulated by local non-adrenergic mechanisms during hypoxia.     

Malate degradation by Schizosaccharomyces yeasts included in alginate beads

Schizosaccharomyces yeasts can be used for deacidification of grape musts. To this aim, we studied malic acid degradation by yeasts included in double layer alginate beads in a bubble column reactor. Use of immobilized micro-organisms allowed a continuous process with high dilution rates giving a deacidification capacity of 0.032 g of malate/hour/dm³/g of beads. The pneumatic agitation was very convenient in this case.List of Symbols D h^–1 Dilution rate for continuous culture - h Residence time for continuous culture - dM/dt kg/(m³ · h) Rate of degradation of malic acid - dS/dt kg/(m³ · h) Rate of consumption of glucose - _max h^–1 Maximal specific rate of growth     

Evaluation of a model for the effects of substrate interactions on the kinetics of reductive dehalogenation

The effects of primary electron-donor and electron-acceptor substrates on the kinetics of TCA biodegradation in sulfate-reducing and methanogenic biofilm reactors are presented. Of the common anaerobic electron-donor substrates that were tested, only formate stimulated the TCA biodegradation rate in both reactors. In the sulfate-reducing reactor, glucose also stimulated the reaction rate. The effects of formate and sulfate on TCA biodegradation kinetics were analyzed using a model for primary substrate effects on reductive dehalogenation. Although some differences between the model and the data are evident, the observed responses of the TCA degradation rate to formate and sulfate were consistent with the model. Formate stimulated the TCA degradation rate in both reactors over the entire range of TCA concentrations that were studied (from 50 g TCA/L to 100 mg TCA/L). The largest effects occurred at high TCA concentrations, where the dehalogenation kinetics were zero order. Sulfate inhibited the first-order TCA degradation rate in the sulfate-reducing reactor, but not in the methanogenic reactor. Molybdate, which is a selective inhibitor of sulfate reduction, stimulated the TCA removal rate in the sulfate-reducing reactor, but had no effect in the methanogenic reactor.     

Purification and characterization of an extracellular β-glucosidase from the anaerobic fungus Piromyces sp. strain E2

An extracellular -glucosidase (EC 3.2.2.21) from the anaerobic fungus Piromyces sp. strain E2 was purified. The enzyme is a monomer with a molecular mass of 45 kDa and a pI of 4.15. The enzyme readily hydrolyzes p-nitrophenyl--d-glycoside, p-nitrophenyl--d-fucoside, cellobiose, cellotriose, cellotetraose and cellopentaose but is not active towards Avicel, carboxymethylcellulose, xylan, p-nitrophenyl--d-galactoside and p-nitrophenyl--d-xyloside. To cleave p-nitrophenyl--d-glucoside the maximum activity is reached at pH 6.0 and 55°C, and the enzyme is stable up to 72 h at 40°C. Activity is inhibited by d-glucurono--lactone, cellobiose, sodium dodecyl sulfate, Hg²⁺ and Cu²⁺ cations. With p-nitrophenyl--d-glycoside, p-nitrophenyl--d-fucoside, and. cellobiose as enzyme substrates, the K _m and V _max balues are 1.5 mM and 25.5 IU·mg^-1, 1.1. mM and 133 IU·mg^-1, and 0.05 mM and 55.6 IU·mg^-1, respectively.     

Physiological control and process kinetics of clavine alkaloid production byClaviceps purpurea

Summary Kinetic parameters of production of clavine alkaloids were evaluated in twoClaviceps purpurea strains. Mutagenesis brought about enhanced resistance of the biosynthetic system towards alkaloids. Addition of glucose into the fermentation medium altered the zero order kinetics of production to activation-inhibition kinetics. The glucose treatment allowed performance of both elymoclavine-inhibitionless and clavine alkaloid-decompositionless fermentations if a combination of fermentation and separation units in a closed loop was used.Nomenlacture k ₁ rate constant of agroclavine synthesis (mg Agro · mg Elymo/l·g DW·day for stage 1, mg Agro/g DW·day for stage 2) - k ₂ parameter describing inhibition of agroclavine formation rate by elymoclavine (mg Elymo/l) - k ₃ specific rate of agroclavine decay (l/g DW·day) - k ₄ maximal specific rate of elymoclavine synthesis (stage 1, 1/g DW·day, stage 2, mg Elymo/g DW·day) - k ₄ ^– maximal specific rate of elymoclavine synthesis in stage 1 (inhibition-activation mechanism) (mg Elymo/g DW·day) - k ₅ physiological constant describing the elymoclavine decay rate (l²/g DW·day·mg Elymo) - k ₅ ^– physiological constant describing the activation of elymoclavine biosynthesis by elymoclavine (mg Elymo/l) - k ₆ physiological constant describing the repression of elymoclavine biosynthesis by elymoclavine (mg Elymo/l) - k ₇ maximal specific growth rate (1/day) - k ₈ specific rate of biomass decay (l/g DW·day) - A agroclavine concentration (mg/l) - E elymoclavine concentration (mg/l) - r _A specific rate of agroclavine biosynthesis (mg Agro/g DW·day) - r _E specific rate of elymoclavine biosynthesis (mg Elymo/g DW·day) - r _i specific rate of alkaloid biosynthesis (mg alkaloid/g DW·day) - X dry biomass concentration (g/l) - specific growth rate (1/day) Abbreviations Agro agroclavine - Elymo elymoclavine - Chano chanoclavine - DW dry weight of biomass     

Physiological and Biochemical Analysis of the Transformants of Aerobic Methylobacteria Expressing the dcmA Gene of Dichloromethane Dehalogenase

Transformants of Methylobacterium dichloromethanicum DM4 (DM4-2cr^–/pME 8220 and DM4-2cr^–/pME8221) and of Methylobacterium extorquens AM1 (AM1/pME8220 and AM1/pME8221) that express the dcm A gene of dichloromethane dehalogenase undergo lysis when incubated in the presence of dichloromethane and are sensitive to acidic shock. The lysis of the transformants was found to be related neither to the accumulation of Cl^– ions, CH₂O, or HCOOH, nor to the impairment of glutathione synthesis or to the disturbance of intracellular pH homeostasis. The (exo^–) Klenow fragment–mediated incorporation of [-³²P]dATP into the DNA of the transformants DM4-2cr^–/pME8220 and AM1/pME8220 was considerably greater when the transformed cells were incubated with CH₂Cl₂ than when they were incubated with CH₃OH, indicating the occurrence of a significant increase in the total length of gaps. At the same time, the strain AM1 (which lacks dichloromethane dehalogenase) and the dichloromethane-degrading strain DM4 incubated with CH₂Cl₂ showed an insignificant increase in the total length of the gaps. The transformed cells are likely to lyse due to the relatively inefficient repair of DNA lesions that are induced in response to the alkylating action of S-chloromethylglutathione, an intermediate product of CH₂Cl₂ degradation. The data obtained suggest that the bacterial mineralization of dichloromethane requires an efficient DNA repair system.