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.     

Extracellular accumulation of recombinant protein by Escherichia coli in a defined medium

Extracellular accumulation of recombinant proteins in the culture medium of Escherichia coli is desirable but difficult to obtain. The inner or cytoplasmic membrane and the outer membrane of E. coli are two barriers for releasing recombinant proteins expressed in the cytoplasm into the culture medium. Even if recombinant proteins have been exported into the periplasm, a space between the outer membrane and the inner membrane, the outer membrane remains the last barrier for their extracellular release. However, when E. coli was cultured in a particular defined medium, recombinant proteins exported into the periplasm could diffuse into the culture medium automatically. If a nonionic detergent, Triton X-100, was added in the medium, recombinant proteins expressed in the cytoplasm could also be released into the culture medium. It was then that extracellular accumulation of recombinant proteins could be obtained by exporting them into the periplasm or releasing them from the cytoplasm with Triton X-100 addition. The tactics described herein provided simple and valuable methods for achieving extracellular production of recombinant proteins in E. coli.     

Intracytoplasmic membrane production inEscherichia coli O111a1: Nutritional parameters

Escherichia coli O111a₁ ceased growth prematurely and accumulated intracytoplasmic membrane at 42°C in an amino acids-mineral salts medium. The amount of membrane formed appeared to be proportional to the concentration of amino acids in the medium—the greater the concentration of amino acids in the medium, the greater the membrane production.E. coli O111a₁, did not grow at 42°C in glucose-, glycerol- or acetate-mineral salts medium, but mesosome-like structures were produced in glucose-grown cells and some intracytoplasmic membrane in cells grown on glycerol and acetate. Supplementation of the glucose medium with pantothenate and/or thiamine permitted normal growth. The vitamins did not restore growth of the mutant in glycerol or acetate, but intracytoplasmic membrane production was increased, especially in glycerol. Amino acids plus glucose supported normal growth with no membrane production. Glycerol and acetate had no effect on the growth in the amino acids medium, but stimulated the accumulation of membrane.     

Band 3 tyr-phosphorylation in normal and glucose-6-phospate dehydrogenase-deficient human erythrocytes

Artificial transformation of Escherichia coli with plasmid DNA in presence of CaCl₂ is a widely used technique in recombinant DNA technology. However, exact mechanism of DNA transfer across cell membranes is largely obscure. In this study, measurements of both steady state and time-resolved anisotropies of fluorescent dye trimethyl ammonium diphenyl hexatriene (TMA-DPH), bound to cellular outer membrane, indicated heat-pulse (0°C→42°C) step of the standard transformation procedure had lowered considerably outer membrane fluidity of cells. The decrease in fluidity was caused by release of lipids from cell surface to extra-cellular medium. A subsequent cold-shock (42°C→0°C) to the cells raised the fluidity further to its original value and this was caused by release of membrane proteins to extra-cellular medium. When the cycle of heat-pulse and cold-shock steps was repeated, more release of lipids and proteins respectively had taken place, which ultimately enhanced transformation efficiency gradually up to third cycle. Study of competent cell surface by atomic force microscope showed release of lipids had formed pores on cell surface. Moreover, the heat-pulse step almost depolarized cellular inner membrane. In this communication, we propose heat-pulse step had two important roles on DNA entry: (a) Release of lipids and consequent formation of pores on cell surface, which helped DNA to cross outer membrane barrier, and (b) lowering of membrane potential, which facilitated DNA to cross inner membrane of E. coli.     

Cyclic antimicrobial R-, W-rich peptides: the role of peptide structure and <Emphasis Type="Italic">E. coli</Emphasis> outer and inner membranes in activity and the mode of action

This study compares the effect of cyclic R-, W-rich peptides with variations in amino acid sequences and sizes from 5 to 12 residues upon Gram negative and Gram positive bacteria as well as outer membrane-deficient and LPS mutant Escherichia coli (E. coli) strains to analyze the structural determinants of peptide activity. Cyclo-RRRWFW (c-WFW) was the most active and E. coli-selective sequence and bactericidal at the minimal inhibitory concentration (MIC). Removal of the outer membrane distinctly reduced peptide activity and the complete smooth LPS was required for maximal activity. c-WFW efficiently permeabilised the outer membrane of E. coli and promoted outer membrane substrate transport. Isothermal titration calorimetric studies with lipid A-, rough-LPS (r-LPS)- and smooth-LPS (s-LPS)-doped POPC liposomes demonstrated the decisive role of O-antigen and outer core polysaccharides for peptide binding and partitioning. Peptide activity against the inner E. coli membrane (IM) was very low. Even at a peptide to lipid ratio of 8/1, c-WFW was not able to permeabilise a phosphatidylglycerol/phosphatidylethanolamine (POPG/POPE) bilayer. Low influx of propidium iodide (PI) into bacteria confirmed a low permeabilising ability of c-WFW against PE-rich membranes at the MIC. Whilst the peptide effect upon eukaryotic cells correlated with the amphipathicity and permeabilisation of neutral phosphatidylcholine bilayers, suggesting a membrane disturbing mode of action, membrane permeabilisation does not seem to be the dominating antimicrobial mechanism of c-WFW. Peptide interactions with the LPS sugar moieties certainly modulate the transport across the outer membrane and are the basis of the E. coli selectivity of this type of peptides.     

Cloning,production and secretion of β-galactosidase inAcetobacter pasteurianus

The gene coding for β-galactosidase fromEscherichia coli was cloned into plasmid pACT71 containing the replicon from plasmid pAC1 fromAcetobacter pasteurianus. E. coli MC4100,E. coli JM105,E. coli LE392.23 andA. pasteurianus 3614 were transformed with the recombinant plasmid pACB815. Cells were cultivated in LB, YPG and M media supplemented with glucose, glycerol, lactose or ethanol and β-galactosidase activity was detected in the cells and in the cultivation medium. The best substrate for production of β-galactosidase was lactose. To release β-galactosidase fromA. pasteurianus cells amino acids were added to the cultivation medium. The highest secretory activity was achieved using 1.5% glycine after 36 h of cultivation in the M medium.     

Influence of acetic acid on the growth of Escherichia coli K12 during high-cell-density cultivation in a dialysis reactor

High-cell-density cultivations of Escherichia coli K12 in a dialysis reactor with controlled levels of dissolved oxygen were carried out with different carbon sources: glucose and glycerol. Extremely high cell concentrations of 190 g/l and 180 g/l dry cell weight were obtained in glucose medium and in glycerol medium respectively. Different behaviour was observed in the formation of acetic acid in these cultivations. In glucose medium, acetic acid was formed during the earlier phase of cultivation. However, in glycerol medium, acetic acid formation started later and was particularly rapid at the end of the cultivation. In order to estimate the influence of acetic acid during these high-cell-density cultivations, the inhibitory effect of acetic acid on cell growth was investigated under different culture conditions. It was found that the inhibition of cell growth by acetic acid in the fermentor was much less than that in a shaker culture. On the basis of the results obtained in these investigations of the inhibitory effect of acetic acid, and the mathematical predictions of cell growth in a dialysis reactor, the influence of acetic acid on high-cell-density cultivation is discussed. Received: 20 May 1997 / Received revision: 12 August 1997 / Accepted: 25 August 1997     

Dynamics of the Antimicrobial Peptide PGLa Action on Escherichia coli Monitored by Atomic Force Microscopy

Summary Atomic force microscopy (AFM) images of living cells in physiological solution were used to monitor the different stages involved in the interaction between Escherichia coli and the antimicrobial peptide PGLa. Damage on bacterial membranes was observed in the past using standard electron microscopy; stiffness measurements and images scanned in physiological solution demonstrate the advantage of AFM for such studies. From force versus separation curve measurements it is possible to determine the variation of the cellular stiffness. PGLa action on components of the cell structure like the outer membrane, the bacterial pili, the peptidoglycan wall and the inner membrane was determined by the comparison of AFM images of bacteria before and after PGLa addition. The interaction of Escherichia coli with PGLa in the culture medium has two stages. The first is characterized by the loss of surface stiffness and the formation of micelles probably originating from the disruption of the outer membrane and the loss of the bacteria’s ability to adhere to the substrates. In the second stage there is further damage, which resulted in total cell rupture. AFM images of bacteria in air and surface roughness measurements were also used to estimate peptide damage.     

Process optimization for large-scale production of TGF-α-PE40 in recombinant Escherichia coli: effect of medium composition and induction timing on protein expression

The effects of medium composition and induction timing on expression of a chimeric fusion protein TGF-α -PE40 (TP-40) in Escherichia coli strain RR1 were examined using a complex medium at several fermentor scales. Two distinctive phases in E. coli catabolism were identified during fermentation based on preferential utilization between protein hydrolysate and glycerol. Maximum specific and volumetric productivities were achieved by inducing the culture when the cells were switching substrate utilization from protein hydrolysate to glycerol. By increasing the yeast extract concentration in the production medium, initiation of the catabolic switch was delayed until high cell mass was achieved. The final titer of TP-40 at the 15-L fermentation scale was doubled from 400 mg L⁻¹ to 850 mg L⁻¹ by increasing the yeast extract concentration from 1% to 4% (w/v) and delaying the time of induction. This fermentation process was rapidly scaled up in 180-L and 800-L fermentors, achieving TP-40 titers of 740 and 950 mg L⁻¹, respectively. Received 26 August 1996/ Accepted in revised form 10 December 1996     

Secretion of the overproduced periplasmic PhoA protein into the medium and accumulation of its precursor in phoA-transformed Escherichia coli strains: involvement of outer membrane vesicles

Various Escherichia coli strains were transformed by multicopy plasmids pHI-1, pHI-7 and pPHOI carrying the entire regulatory and structural phoA sequences. All transformants with the intact pho regulatory system displayed PhoA oversynthesis and secretion into the medium. They also accumulated the alkaline phosphatase precursor localized in the outer membrane fraction. The dynamics of enzyme synthesis and secretion as well as cell cytomorphology during secretion were studied in strain E. coli K12 802 carrying pHI-7 plasmid. PhoA protein was shown to be selectively released into the medium in vesicles budding from outer membrane.The authors are with the institute of Biochemistry and Physiology of Microorganisms, USSR Academy of Sciences, 142292 Puschino, Moscow Region, USSR.     

Body structure of marine sponges

Summary Specimens of Haliclona elegans (Bowerbank, 1866) are covered by a thin, double layered dermal membrane extending over large subdermal spaces. The pores in the dermal membrane are formed by single porocytes with one or sometimes several pores in the center of the cell. The subjacent tissue shows a faintly developed mesenchyme and numerous big choanocyte chambers projecting into lacunar spaces of the incurrent canal system. The outer surface of the chambers is directly covered by the pinacocyte epithelium of the incurrent canal wall, which also separates them completely from the mesenchyme. Water influx into the chambers is guaranteed by prosopylar openings in the pinacocyte cover at the outer chamber surface. The chambers are connected to the excurrent canal system in the eurypylous way by wide apopyles, each of which is surrounded by a small ring of flagellated cone cells. About 15% of the choanocyte chambers in H. elegans contain central cells, which are thought to derive from migrating pinacocytes of the canal systems.     

Microencapsulation of yeast cells in the calcium alginate membrane

Summary Cells of Saccharomyces cerevisiae (ATCC 24858) were encapsulated in the calcium alginate membrane and cultured. Swelling of the capsule was prevented by adding 0.2 g CaCl₂ to 1 L growth medium. The dry cell concentration based on the inner volume of the capsule reached 309 g/L, which was much higher than could be obtained by cell entrapment. All the cells remained inside the capsule during the cultivation. The flux of CO₂ through the capsule membrane increased approximately twice by adding a nonionic surfactant to the CaCl₂ solution during the step of capsule formation.     

RelA1 gene control of Escherichia coli lipid structure and cell performance during glucose limited fed-batch conditions

At increasing glucose limitation, typical for fed-batch cultivation performance, cultivation of Escherichia coli (relA1) results in development of a lipid structure that radically differs from the wild type and is characterised by accumulation of neutral phospholipids and saturated fatty acids. The mutant can, furthermore, not change the level of cardiolipin, which is generally the hallmark of changes to severe glucose limitation. The result suggests an increased negative control in the mutant with respect to the flux to phosphatidyl glycerol and cardolipin as well as to unsaturated fatty acids. Opposite to the wild type, the cardiolipin-depleted membrane is more fragile with respect to sonication and osmotic chock, at severe limitation, and results in extensive foaming during the process. Protein leakage and cell lysis is, however, lower in the mutant most likely due to the increased amounts of saturated fatty acids, which might be a possible strategy to overcome the reduced amounts of membrane-strengthening cardiolipin. The membrane potential of the outer surface is negative, however less negative for the mutant. This was supported by aqueous two-phase extraction experiments which, furthermore indicated a difference in outer surface hydrofobicity. These findings suggest that the relA1 gene has a defined, but ppGpp-independent, role in cells with a slowly decreasing metabolism of glucose to control the membrane morphology.     

A two-compartment cell entrapment bioreactor with three different holding times for cells,high and low molecular weight compounds

A new bioreactor for animal cell cultivation employs two compartments for cells and medium respectively. The two chambers are separated by an ultrafiltration membrane. Cells and solution of collagen or collagen/chitosan mixture were loaded to the cell chamber and were allowed to form gel inside. Contraction of the cell-laden gel occurred subsequently to create a new zone in the cell chamber. In such a bioreactor cells are retained in the reactor, the high molecular product(s) accumulate in the cell chamber, while the small molecular weight nutrients and metabolites are replenished and removed from the medium chamber. By adjusting the flow rates for cell and medium chambers, the resident time for cells, high and low molecular weight components of the system can be manipulated separately. The new bioreactor, in both flat-bed and hollow-fiber configurations, was used to cultivate recombinant human cell, 293, for Protein C production over 60 to 90 days.     

Development of production and purification processes of recombinant fragment of pneumococcal surface protein A in <Emphasis Type="Italic">Escherichia coli</Emphasis> using different carbon sources and chromatography sequences

Pneumococcal surface protein A (PspA) is essential for Streptococcus pneumoniae virulence and its use either as a novel pneumococcal vaccine or as carrier in a conjugate vaccine would improve the protection and the coverage of the vaccine. Within this context, the development of scalable production and purification processes of His-tagged recombinant fragment of PspA from clade 3 (rfPspA3) in Escherichia coli BL21(DE3) was proposed. Fed-batch production was performed using chemically defined medium with glucose or glycerol as carbon source. Although the use of glycerol led to lower acetate production, the concentration of cells were similar at the end of both fed-batches, reaching high cell density of E. coli (62 g dry cell weight/L), and the rfPspA3 production was higher with glucose (3.48 g/L) than with glycerol (2.97 g/L). A study of downstream process was also carried out, including cell disruption and clarification steps. Normally, the first chromatography step for purification of His-tagged proteins is metal affinity. However, the purification design using anion exchange followed by metal affinity gave better results for rfPspA3 than the opposite sequence. Performing this new design of chromatography steps, rfPspA3 was obtained with 95.5% and 75.9% purity, respectively, from glucose and glycerol culture. Finally, after cation exchange chromatography, rfPspA3 purity reached 96.5% and 90.6%, respectively, from glucose and glycerol culture, and the protein was shown to have the expected alpha-helix secondary structure.     

Phenol-induced membrane changes in free and immobilized Escherichia coli

Summary Membranes of Escherichia coli cells grown in the presence of phenol were examined after isolation of the cytoplasmic and outer membrane fractions. Both membrane types showed reduced lipid-to-protein ratios compared to cells grown without phenol. Phenol-induced differences in the expression of individual proteins of the outer membrane, probably involved in the uptake of iron, were expressed in smaller quantities after phenol addition. Growth in the presence of phenol increased the respiratory activity of the cytoplasmic membrane, whereas the direct inhibition of O₂ consumption by phenol was not affected by the presence of this compound in the growth medium. E. coli cells grown entrapped in calcium alginate showed low lipid-to-protein ratios even without phenol in the growth medium. Immobilization of cells also markedly changed the protein pattern of the outer membrane. Offprint requests to: H.-J. Rehm     

A novel bioreactor for immobilized phototrophs

A novel configuration of photobioreactor is described in which filaments of alginate containing immobilized cells of a leaky mutant of Dunaliella parva are wound round a central light well which is located within a glass outer chamber so that a liquid medium is caused to flow in the annular space between the outside chamber and the alginate filaments. Glycerol production by D. parva was maintained for 700 h and the highest concentration of glycerol attained was approx. 12 mg l⁻¹.     

Simple fed-batch technique for high cell density cultivation of Escherichia coli

A simple fed-batch process for high cell density cultivation of Escherichia coli TG1 was developed. A pre-determined feeding strategy was chosen to maintain carbon-limited growth using a defined medium. Feeding was carried out to increase the cell mass concentration exponentially in the bioreactor controlling biomass accumulation at growth rates which do not cause the formation of acetic acid (μ < μ_crit). Cell concentrations of 128 and 148 g per 1 dry cell weight (g 1⁻¹ DCW) were obtained using glucose or glycerol as carbon source, respectively.     

Outer membrane proteins of thebacteroides fragilis group

The Triton-insoluble outer membrane proteins of members of the obligately anaerobicBacteroides fragilis group were examined by sodium dodecyl sulfate-polyacrylamide gel electrophoresis. The application of previously published methods for the preparation of outer membranes from these anaerobes led to relatively low recoveries of outer membrane material. Additionally, the outer membrane recovered was not qualitatively or quantitatively representative of the total outer membrane. A method previously devised for the isolation of the outer membrane proteins fromEscherichia coli was used. By this method, the members of theB. fragilis group were found to possess a striking capacity to alter their cell-surface proteins in response to cultivation in different media.     

Kinetics of glycerol uptake by the perfused rat liver Membrane transport, phosphorylation and effect on NAD redox level

The kinetics of glycerol uptake by the perfused rat liver were determined according to a model which includes membrane transport, intracellular phosphorylation and competitive inhibition of glycerol phosphorylation by l-glycerol 3-phosphate. The membrane transport obeys first-order kinetics at concentrations below 10 mM in the affluent medium. The K_m of the glycerol phosphorylation was was 10 μM and the K_i of the l-glycerol 3-phosphate inhibition was 50 μM. The maximum activity (V) was 3.70 μmoles/min per g liver wet wt. These results are similar to in vitro kinetics of the glycerol kinase, except that K_i was found to be somewhat lower in the intact organ. At low glycerol concentrations, gradient exists across the liver cell membrane.The increase in the lactate to pyruvate concentration ratio during glycerol metabolism is related to the actual concentration of l-glycerol 3-phosphate, not to the rate of glycerol uptake.