Osmotic fragility of the group A streptococcal L form

The osmotic fragility, expressed in terms of survival, of two group A streptococcal L-form strains was examined by suspending the L form in sodium chloride and sucrose solutions of graded concentrations. An immediate and marked reduction in viability followed suspension in sodium chloride solutions of less than 0.7m. A wide distribution of osmotic fragility within the L-form population was observed. The two L-form strains (GL-8 and AED) differed in that the AED L-form strain appeared to be consistently more resistant to osmotic lysis, and survived considerably better in sodium chloride solutions up to 90 minutes. Sucrose solutions of tonicities comparable to those of the sodium chloride solutions used, however, stabilized the labile GL-8 L form completely. Magnesium chloride (0.05m) and serum (10% v/v) substantially increased L-form survival in sodium chloride. The results are interpreted to indicate a difference in the cell envelope of the two L-form strains, the AED limiting membrane possessing a greater intrinsic stability. The significantly greater resistance to sonic oscillation of the AED L form as compared to the GL-8 L form, is in agreement with and supports this conclusion. The possibility that the difference in physical properties of the two L-form strains is related to a difference in chemical composition of their limiting envelopes is discussed.The author wishes to thank Dr. W. Hijmans for his interest and advice, and Miss H. L. Ensering and Miss M. J. W. Kastelein for technical assistance.     

Oscillations of the energy gap for the initial electron-transfer step in bacterial reaction centers

Oscillations in the electrostatic energy gap [V_elec(t)] for electron transfer from the primary electron donor (P) to the adjacent bacteriochlorophyll (B) in photosynthetic bacterial reaction centers are examined by molecular-dynamics simulations. Autocorrelation functions of V_elec in the reactant state (PB) include prominent oscillations with an energy of 17 cm^–1. This feature is much weaker if the trajectory is propagated in the product state P⁺B^–. The autocorrelation functions also include oscillations in the regions of 5, 80 and 390 cm^–1 in both states, and near 25 and 48 cm^–1 in P⁺B^–. The strong 17-cm^–1 oscillation could involve motions that modulate the distance between P and B, because a similar oscillation occurs in the direct electrostatic interactions between the electron carriers.     

Stochastic late effects after partial body irradiation in diagnostic radiology: Evaluation of approximate data

Summary The paper describes a method to estimate the risk of inducing a malignant disease by the highly nonuniform partial body X-irradiation as performed in diagnostic radiological examinations. The cumulative probability,p, for the development of a radiation-induced malignant neoplasm is obtained from the equationp =G _t E _s, whereE _s is the energy imparted to the soft tissues of trunk and head during a special radiological procedure.G _t is the mean integral incidence function for trunk and head, reflecting the cancer inducibility of organs and tissues in trunk and head,G _t 0.3 kJ^–1. The value ofG _t was obtained from mortality risk factors for the different tissues at risk, adopted in ICRP Publication 26, 1977.The energy,E, imparted to the body in typical radiographic procedures is in the range of 1–30 mJ, going up to about 1 J in an extensive fluoroscopic examination of the gastrointestinal tract. The corresponding values forp are about 10^–6 to 10^–5, in extensive examinations 10^–4. As to a radiograph of chest, the method described in this paper yields practically the same value forp as the Monte Carlo calculation, using the MIRD phantom and the relevant mortality risk factors.     

Dynamics of production oftrans-zeatin andtrans-zeatin riboside by immobilized cytokinin-autonomous and cytokinin-dependent tobacco cells

Two strains of cultured tobacco cells (Nicotiana tabacum L. cv. Wisconsin 38) differing in their requirement for exogenous cytokinins (cytokinin-dependent and cytokinin-autonomous) were immobilized on polyphenylenoxide (Sorfix) activated with glutaraldehyde. Columns packed with immobilized cells were continually eluted with diluted Murashige and Skoog's medium lacking or supplemented with synthetic cytokinin (6-benzylaminopurine; BA). Purified samples of column eluates were fractionated by HPLC, andtrans-zeatin (t-Z) andtrans-zeatin riboside (t-ZR) content was estimated by enzyme immunoassay. Both cytokinin-autonomous and cytokinin-dependent tobacco cells produced and excretedt-Z and its riboside, and there were significant quantitative differences between the strains. The steady-state excretion rate oft-Z was 19.8 ng · g^–1 dw · h^–1 and 4 ng · g^–1 dw · h^–1, respectively, and that oft-ZR 4 ng · g^–1 dw · h^–1 and 1 ng · g^–1 dw · h^–1, respectively. Exposure of cytokinin-dependent cells to BA after 72 h of starving for this synthetic cytokinin caused temporary increase in excretion of both zeatin and its riboside. After the application of 5 M BA for 24 h, the excretion rate oft-ZR reached 5 ng · g^–1 dw · h^–1 (5-fold increase), and that oft-Z achieved 12 ng · g^–1 dw · h^–1 (3-fold increase). The elevation oft-Z excretion was delayed about 13 h compared witht-ZR excretion, which started increasing almost immediately after BA application. A pulse of BA in lower concentration (1.5 M for 30 h) provoked lower response.     

Energy cost and energy sources in karate

Energy costs and energy sources in karate (wado style) were studied in eight male practitioners (age 23.8 years, mass. 72.3 kg, maximal oxygen consumption (VO_2max) 36.8 ml · min^–1 · kg^–1) performing six katas (formal, organized movement sequences) of increasing duration (from approximately. 10 s to approximately 80 s). Oxygen consumption (VO₂) was determined during pre-exercise rest, the exercise period and the first 270 s of recovery in five consecutive expired gas collections. A blood sample for lactate (la^–) analysis was taken 5 min after the end of exercise. The overall amount of O₂ consumed during the exercise and in the following recovery increased linearly with the duration of exercise (t) from approximately 1.51 (for t equal to 10.5 s (SD 1.6)) to approximately 5.81, for t equal to 81.5 s (SD 1.0). The energy release from la^– production (VO_21a ^–) calculated assuming that an increase of 1 mmol · l^–1 la^– corresponded to a VO₂ of 3 mlO₂ · kg^–1 was negligible for t equal to or less than 20 s and increased to 17.3 ml · kg^–1 (la^– = 5.8 mmol · l^–1 above resting values) for t equal approximately to 80 s. The overall energy requirement (VO_2eq) as given by the sum of VO₂ and VO_2la ^– was described by VO_2eq = 0.87 + 0.071 · t (n = 64; r ² = 0.91), where VO_2eq is in litres and t in seconds. This equation shows that the metabolic power (VO_2eq · t ^–1) for this karate style is very high: from approximately 9.51 · min^–1 for t equal to 10 s to approximately 4.91 · min^–1 for t equal to 80 s, i.e. from 3.5 to 1.8 times the subjects' VO_2max. The fraction of VO_2eq derived from the amount of O₂ consumed during the exercise increased from 11% for t equal to 10 s to 41 % for t equal to 80 s whereas VO_21a ^– was negligible far t equal to or less than 20 s and increased to 13 % o for t equal to 80 s. The remaining fraction (from 90% for t equal to 10 s to 46% for t equal to 80 s), corresponding to the amount of O₂ consumed in the recovery after exercise, is derived from anaerobic alactic sources, i.e. from net splitting of high energy phosphates during the exercise.     

Mutants of Myxococcus xanthus insensitive to glycerol-induced myxospore formation

Mutants of Myxococcus xanthus FB_t unable to form myxospores in response to 0.5 M glycerol arise spontaneously with a frequency of 1–3×10^–5. These mutants are designated glc. Ultraviolet mutagenesis increases the frequency to a maximum of 7% of the survivors. The reversion frequency following ultraviolet irradiation of spontaneous glc mutants is less than 10^–3. Of four glc mutants examined, none form myxospores in response to the alternative inducers, ethylene glycol and dimethyl sulphoxide. One glc mutant is induced by 1.5 M glycerol; strain FB_t responds to this glycerol concentration with low efficiency myxospore formation. Strain FB_t and glc mutants all produce myxospores with low efficiency in response to phenyl ethanol. Of 117 glc mutants tested, 109 form fruiting bodies containing mature myxospores; thus, mutations to the glc phenotype do not normally block myxospore formation within the fruiting cycle of the organism.     

Isolation of <Emphasis Type="BoldItalic">Serratia marcescens</Emphasis> as a chondroitinase-producing bacterium and purification of a novel chondroitinase AC

A strain of Serratia marcescens that produced chondroitinase was isolated from soil. It produced a novel chondroitinase AC, which was purified to homogeneity. The enzyme was composed of two identical subunits of 35 kDa as revealed by SDS-PAGE and gel filtration. The isoelectric point for the chondroitinase AC was 7.19. Its optimal activity was at pH 7.5 and 40 °C. The purified enzyme was active on chondroitin sulfates A and C and hyaluronic acid, but was not with chondroitin sulfate B (dermatan sulfate), heparin or heparan sulfate. The apparent K_m and V_max of the chondroitinase AC for chondroitin sulfate A were 0.4 mg ml^–1 and 85 mmol min^–1 mg^–1, respectively, and for chondroitin sulfate C, 0.5 mg ml^–1 and 103 mmol min^–1 mg^–1, respectively.     

Study of the Mechanism of Action of p-Chloromercuribenzoate on Endonuclease from the Bacterium Serratia marcescens

The mechanism of action of p-chloromercuribenzoate (PCMB) on Serratia marcescens nuclease was investigated. The analysis showed that PCMB forms complexes with DNA. Binding of C₇H₅O₂Hg⁺ to DNA changes the secondary structure of the DNA. These changes alter the enzymatic activity of S. marcescens nuclease, which was previously found to be sensitive to the secondary structure of the substrates. The nuclease activity was either suppressed or stimulated in the presence of PCMB depending on the C₇H₅O₂Hg⁺ to nucleotide equivalent ratio. Binding of C₇H₅O₂Hg⁺ to DNA did not form an abortive enzyme–substrate complex. Binding of Mg²⁺ to the C₇H₅O₂Hg–DNA complex caused appropriate changes in secondary structure of the substrate. Since Mg²⁺ and C₇H₅O₂Hg⁺, though differing in the type of metal cation, are similar in their mechanisms of influence on enzymatic activity of S. marcescens nuclease, the identity of other metal-containing effectors in their mechanism of action on Serratia marcescens nuclease is assumed.     

Chemolithoautotrophy in the marine,magnetotactic bacterial strains MV-1 and MV-2

Magnetite-producing magnetotactic bacteria collected from the oxic–anoxic transition zone of chemically stratified marine environments characterized by O₂/H₂S inverse double gradients, contained internal S-rich inclusions resembling elemental S globules, suggesting they oxidize reduced S compounds that could support autotrophy. Two strains of marine magnetotactic bacteria, MV-1 and MV-2, isolated from such sites grew in O₂-gradient media with H₂S or thiosulfate (S₂O₃^2–) as electron sources and O₂ as electron acceptor or anaerobically with S₂O₃^2– and N₂O as electron acceptor, with bicarbonate (HCO₃^–)/CO₂ as sole C source. Cells grown with H₂S contained S-rich inclusions. Cells oxidized S₂O₃^2– to sulfate (SO₄^2–). Both strains grew microaerobically with formate. Neither grew microaerobically with tetrathionate (S₄O₆^2–), methanol, or Fe²⁺ as FeS, or siderite (FeCO₃). Growth with S₂O₃^2– and radiolabeled ¹⁴C-HCO₃^– showed that cell C was derived from HCO₃^–/CO₂. Cell-free extracts showed ribulose 1,5-bisphosphate carboxylase/oxygenase (RubisCO) activity. Southern blot analyses indicated the presence of a form II RubisCO (cbbM) but no form I (cbbL) in both strains. cbbM and cbbQ, a putative post-translational activator of RubisCO, were identified in MV-1. MV-1 and MV-2 are thus chemolithoautotrophs that use the Calvin–Benson–Bassham pathway. cbbM was also identified in Magnetospirillum magnetotacticum. Thus, magnetotactic bacteria at the oxic–anoxic transition zone of chemically stratified aquatic environments are important in C cycling and primary productivity.     

Influence of operational parameters in the flocculation and production ofLactobacillus plantarum

Summary The influence of different operational parameters, such as the dilution rate (D) and the bleeding rate (B), in the production of a flocculent strain ofLactobacillus plantarum was studied. The effect of the dilution rate was demonstrated to be related to the lactic acid concentration inside the reactor. The effect of the bleeding rate was shown to be critical in the stabilization of the operation (due to a better pH control). It also allowed a continuous recovery of cells outside the reactor. Viability testing of the lactic starter cultures showed that operation with cell purge increased the viability of the starter cultures obtained.Nomenclature B Bleeding rate, h^–1 - D Dilution rate, h^–1 - F Feed flow rate, L h^–1 - I Feed velocity, m h^–1 - Specific growth rate, h^–1 - v Lactic acid specific productivity, g g^–1 h^–1 - P Product concentration (lactic acid), g L^–1 - P _out Product concentration leaving the system, g L^–1 - Q _b Bleeding flow rate, L h^–1 - R Recirculation velocity, m h^–1 - S Substract concentration, g L^–1 - t Time, h - T _p Time of ascensional flow (length of the column/total ascensional velocity), h - T _r Residence time (1/D), h - V Volume of the reactor, L - X Cell concentration, g L^–1 - X _out Cell concentration leaving the system, g L^–1     

Electrical effects of potassium and bicarbonate on proximal tubule cells ofNecturus

Summary The effects of stepwise concentration changes of K⁺ and HCO ₃ ^– in the basolateral solution on the basolateral membrane potential (V _bl) of proximal tubule cells of the doubly-perfusedNecturus kidney were examined using conventional microelectrodes. Apparent transference numbers were calculated from changes inV _bl after alterations in external K⁺ concentration from 1.0 to 2.5mm (t _{K, 1.0–2.5}), 2.5 to 10, and in external HCO ₃ ^– concentration (at constant pH) from 5 to 10mm (t _{HCO3, 5–10}), 10 to 20, or 10 to 50.t _{K, 2.5–10} was 0.38±0.02 under control conditions but was sharply reduced to 0.08±0.03 (P>0.001) by 4mm Ba⁺⁺. This concentration of Ba⁺⁺ reducedV _bl by 9±1 mV (at 2.5 external K⁺). Perfusion with SITS (5×10^–4 m) for 1 hr hyperpolarizedV _bl by 10±3 mV and increasedt _{K, 2.5–10} significantly to 0.52±0.01 (P<0.001). Ba⁺⁺ application in the presence of SITS depolarizedV _bl by 22±3 mV. In control conditionst _{HCO3, 10–50} was 0.63±0.05 and was increased to 0.89±0.07 (P<0.01) by Ba⁺⁺ but was decreased to 0.14±0.02 (P<0.001) by SITS. In the absence of apical and basolateral chloride, the response ofV _bl to bicarbonate was diminished but still present (t _{HCO3, 10–20} was 0.35±0.03). Intracellular pH, measured with liquid ion-exchange microelectrodes, increased from 7.42±0.19 to 7.57±0.17 (P<0.02) when basolateral bicarbonate was increased from 10 to 20mm at constant pH. These data show that the effects of bicarbonate onV _bl are largely independent of effects on the K⁺ conductance and that there is a significant current-carrying bicarbonate pathway in the basolateral membrane. Hence, both K⁺ and HCO ₃ ^– gradients are important in the generation ofV _bl, and their relative effects vary reciprocally.     

Microtubular structures in group D streptococcal L-forms

Summary Microtubular structures, apparently continuous with the plasmalemma, have been observed in thin sections of two strains of group D streptococcal L-forms. The tubules had an external diameter of about 250 Å and a hollow core 100–150 Å in diameter. The tubules were found protruding either into or out of the L-form cells and were only found in cultures growing in the presence of penicillin.     

Limited degradation of industrial,synthetic and natural lignins by Serratia marcescens

Summary Serratia marcescens was found to degrade kraft lignin by only 15%. When ¹⁴C-radiolabelled lignocelluloses and DHP lignins were used as substrates the bacterium mineralized to ¹⁴CO₂ only 1.1–1.9% and 0.4–0.8% of the lignins respectively. However, some 44.4% of the ¹⁴C--DHP lignin was recovered as soluble radiolabelled products.     

Experimental study of 60Co behaviour in Tejo River sediments

The objective of this study was to obtain information on the transfer of radiocobalt in freshwater environments that can be used to predict its environmental distribution. The sediment-water behaviour of ⁶⁰Co in freshwater systems was studied through adsorption and desorption experiments undertaken using sediments and water from Fratel Reservoir in the Tejo River. The suspended sediment concentrations (C_s: 500–2000 mg 1^–1) and Co distribution coefficient (K_d) were inversely related: K_d = 2211–2001 ln [C_s]; K_d ranged from 4000 to 8000 ml g^–1. With a suspended sediment concentration of 1000 mg 1^–1, the ⁶⁰Co concentration remaining in solution (C_t) was given by: C_t = 49.4 e^–0.584t + 46.3 e^–0.014t; where t is the time in days and the half-life periods are 1.2 and 50 days. In a closed system, desorption of ⁶⁰Co could be described by a one-component relation with a half-life of 104 days, and a two component relation (half-life 5 hours and 45 days) in an open system. In river water the ⁶⁰Co was found to be almost 100% in cationic forms, however, in the presence of sediment there was a decrease in the proportion of cationic forms (to 50%), with some anionic forms appearing.     

Inorganic mercury (Hg2+) transport through lipid bilayer membranes

Summary Diffusion of inorganic mercury (Hg²⁺) through planar lipid bilayer membranes was studied as a function of chloride concentration and pH. Membranes were made from egg lecithin plus cholesterol in tetradecane. Tracer (²⁰³Hg) flux and conductance measurements were used to estimate the permeabilities to ionic and nonionic forms of Hg. At pH 7.0 and [Cl^–] ranging from 10–1000mm, only the dichloride complex of mercury (HgCl₂) crosses the membrane at a significant rate. However, several other Hg complexes (HgOHCl, HgCl ₃ ^– and HgCl ₄ ^2– ) contribute to diffusion through the aqueous unstirred layer adjacent to the membrane. The relation between the total mercury flux (J _Hg), Hg concentrations, and permeabilities is: 1/J _Hg=1/P ^ul[Hg ^t ]+1/P ^m [HgCl₂], where [Hg ^t ] is the total concentration of all forms of Hg,P ^ul is the unstirred layer permeability, andP ^m is the membrane permeability to HgCl₂. By fitting this equation to the data we find thatP ^m =1.3×10^–2 cm sec^–1. At Cl^– concentrations ranging from 1–100mm, diffusion of Hg ^t through the unstirred layer is rate limiting. At Cl^– concentrations ranging from 500–1000mm, the membrane permeability to HgCl₂ becomes rate limiting because HgCl₂ comprises only about 1% of the total Hg. Under all conditions, chemical reactions among Hg²⁺, Cl^– and/or OH^– near the membrane surface play an important role in the transport process. Other important metals, e.g., Zn²⁺, Cd²⁺, Ag⁺ and CH₃Hg⁺, form neutral chloride complexes under physiological conditions. Thus, it is likely that chloride can facilitate the diffusion of a variety of metals through lipid bilayer and biological membranes.     

“Diffusion” of microorganisms in calcium alginate beads

Summary The leakage of Serratia marcescens cells immobilised in Ca-alginate beads was quantified and the experimental values fitted to the pore diffusion model in order to obtain the biomass diffusion coefficient (D _x). This coefficient was then determined, resulting a value of 0.45 10^–7 cm² s^–1 at the beginning of the fermentation process. The variation of this coefficient, together with the porosity of the particles (_i), were also determined all along the process.     

Improvement of a mammalian cell culture process by adaptive,model-based dialysis fed-batch cultivation and suppression of apoptosis

Both conventional and genetic engineering techniques can significantly improve the performance of animal cell cultures for the large-scale production of pharmaceutical products. In this paper, the effect of such techniques on cell yield and antibody production of two NS0 cell lines is presented. On the one hand, the effect of fed-batch cultivation using dialysis is compared to cultivation without dialysis. Maximum cell density could be increased by a factor of ~5–7 by dialysis fed-batch cultivation. On the other hand, suppression of apoptosis in the NS0 cell line 6A1 bcl-2 resulted in a prolonged growth phase and a higher viability and maximum cell density in fed-batch cultivation in contrast to the control cell line 6A1 (100)3. These factors resulted in more product formation (by a factor ~2). Finally, the adaptive model-based OLFO controller, developed as a general tool for cell culture fed-batch processes, was able to control the fed-batch and dialysis fed-batch cultivations of both cell lines.Abbreviations A membrane area (dm²) - c _Glc,F glucose concentration in nutrient feed (mmol L^–1) - c _Glc,FD glucose concentration in dialysis feed (mmol L^–1) - c _Glc,i glucose concentration in inner reactor chamber (mmol L^–1) - c _Glc,o glucose concentration in outer reactor chamber (dialysis chamber) (mmol L^–1) - c _Lac,FD lactate concentration in dialysis feed (mmol L^–1) - c _Lac,i lactate concentration in inner reactor chamber (mmol L^–1) - c _Lac,o lactate concentration in outer reactor chamber (dialysis chamber) (mmol L^–1) - c _LS,FD limiting substrate concentration in dialysis feed (mmol L^–1) - c _LS,i limiting substrate concentration in inner reactor chamber (mmol L^–1) - c _LS,o limiting substrate concentration in outer reactor chamber (dialysis chamber) (mmol L^–1) - c _Mab monoclonal antibody concentration (mg L^–1) - F _D feed rate of dialysis feed (L h^–1) - F _Glc feed rate of nutrient concentrate feed (L h^–1) - K _d maximum death constant (h^–1) - k _d,LS death rate constant for limiting substrate (mmol L^–1) - k _Glc monod kinetic constant for glucose uptake (mmol L^–1) - k _Lac monod kinetic constant for lactate uptake (mmol L^–1) - k _LS monod kinetic constant for limiting substrate uptake (mmol L^–1) - K _Lys cell lysis constant (h^–1) - K _S,Glc monod kinetic constant for glucose (mmol L^–1) - K _S,LS monod kinetic constant for limiting substrate (mmol L^–1) - µ cell-specific growth rate (h^–1) - µ _d cell-specific death rate (h^–1) - µ _d,min minimum cell-specific death rate (h^–1) - µ _max maximum cell-specific growth rate (h^–1) - P _Glc membrane permeation coefficient for glucose (dm h^–1) - P _Lac membrane permeation coefficient for lactate (dm h^–1) - P _LS membrane permeation coefficient for limiting substrate (dm h^–1) - q _Glc cell-specific glucose uptake rate (mmol cell^–1 h^–1) - q _Glc,max maximum cell-specific glucose uptake rate (mmol cell^–1 h^–1) - q _Lac cell-specific lactate uptake/production rate (mmol cell^–1 h^–1) - q _Lac,max maximum cell-specific lactate uptake rate (mmol cell^–1 h^–1) - q _LS cell-specific limiting substrate uptake rate (mmol cell^–1 h^–1) - q _LS,max maximum cell-specific limiting substrate uptake rate (mmol cell ^–1 h^–1) - q _Mab cell-specific antibody production rate (mg cell^–1 h^–1) - q _MAb,max maximum cell-specific antibody production rate (mg cell^–1 h^–1) - t time (h) - V _i volume of inner reactor chamber (culture chamber) (L) - V _o volume of outer reactor chamber (dialysis chamber) (L) - X _t total cell concentration (cells L^–1) - X viable cell concentration (cells L^–1) - Y _Lac/Glc kinetic production constant (stoichiometric ratio of lactate production and glucose uptake) (–)     

Action of hexaamminecobalt on the activity of Serratia marcescens nuclease

Using CD spectroscopic and kinetic analysis, a refined mechanism of Co(NH₃) ₆ ³⁺ action on activity of Serratia marcescens nuclease was elucidated. The mechanism was identical with previously found mechanisms of Mg²⁺ and C₇H₅O₂Hg⁺. Similarly to Mg²⁺ and C₇H₅O₂Hg⁺, Co(NH₃) ₆ ³⁺ binding to the DNA substrate induced changes in the secondary structure which resulted in changes of the enzymatic activity of the S. marcescens nuclease. Upon binding of 0.03 Co(NH₃) ₆ ³⁺ per DNA phosphate, highly polymerized DNA displayed A-form characteristics. The DNA transition from B-form to A-form intermediate was followed by a decrease of the nuclease activity. The diminishing nuclease activity was consistent with diminishing values of Km and Kcat. Co(NH₃)₆ ³⁺ binding to the highly polymerized DNA caused a 1.7–2.8-fold decrease in Km, and 13.3–19.9 decrease in Vmax compared with Mg-DNA complex. A vast excess of Co(NH₃)₆ ³⁺ did not affect the activity of S. marcescens nuclease if the DNA in the assay mixture remained in its B-form conformation. Preincubation of S. marcescens nuclease with Co(NH₃)₆ ³⁺ did not influence the tertiary structure of the enzyme.     

A heuristic approach to fed-batch optimisation of streptokinase fermentation

Previous studies have shown that the rate of formation of streptokinase, a secondary metabolite, in batch fermentation is proportional to the specific growth rate of the biomass, which in turn is inhibited by its substrate and the primary product (lactic acid). These kinetics suggest the suitability of fed-batch operation to increase the yield of streptokinase. A near-optimal feed policy has been calculated by the chemotaxis algorithm, and it shows a substrate feed rate decreasing nonlinearly and vanishing after 11 hours. This is followed by batch fermentation for a further 8 hours, at the end of which 12% more streptokinase is generated than by purely batch fermentation. Further improvements in productivity are possible.List of Symbols k _dh^–1 decay constant for active cells - k _ph^–1 decay constant for streptokinase - K _Igl^–1 inhibition constant for lactic acid - K_S gl^–1 inhibition constant for substrate - M gl^–1 lactic acid concentration - P gl^–1 streptokinase concentration - Q 1h^–1 substrate feed rate - S gl^–1 substrate concentration - S _ingl^–1 inlet concentration of substrate - t h time - t _bh end-point of batch fermentation - t _fh end-point of fed-batch fermentation - V l volume of broth in fermenter - V ₀ l initial value of V (at t=0) - V _ml maximum value of V - X gl^–1 total biomass concentration - X _agl^–1 concentration of active biomass - Y _MX yield coefficient for lactic acid from biomass - Y _PX yield coefficient for streptokinase from biomass - Y _XS yield coefficient for biomass from substrate Greek Letters h^–1 specific growth rate of biomass - _mh^–1 maximum specific growth rate