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  • 1
    Electronic Resource
    Electronic Resource
    Amsterdam : Elsevier
    Enzyme and Microbial Technology 15 (1993), S. 652-656 
    ISSN: 0141-0229
    Keywords: Dihydrofolate reductase ; Escherichia coli ; continuous culture ; methotrexate
    Source: Elsevier Journal Backfiles on ScienceDirect 1907 - 2002
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
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  • 2
    Electronic Resource
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    Amsterdam : Elsevier
    Enzyme and Microbial Technology 16 (1994), S. 240-246 
    ISSN: 0141-0229
    Keywords: Bacillus subtilis ; Escherichia coli ; Fermentation ; Plasmid stability
    Source: Elsevier Journal Backfiles on ScienceDirect 1907 - 2002
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
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  • 3
    ISSN: 0141-0229
    Keywords: 6-aminopenicillanic acid (6-APA) ; DH5 cells ; Escherichia coli ; constitutive; β-lactamase negative ; lactose broth (LB) ; optimization of enzyme production parameters ; pac gene ; penicillin acylase ; plasmid pUSAD2
    Source: Elsevier Journal Backfiles on ScienceDirect 1907 - 2002
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
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  • 4
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    Amsterdam : Elsevier
    Enzyme and Microbial Technology 15 (1993), S. 730-735 
    ISSN: 0141-0229
    Keywords: Escherichia coli ; Molecular chaperones ; heat shock proteins ; protein folding ; recombinant DNA
    Source: Elsevier Journal Backfiles on ScienceDirect 1907 - 2002
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
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  • 5
    ISSN: 0141-0229
    Keywords: Escherichia coli ; computer control ; exponentially fed-batch culture ; penicillin acylase ; penicillin amidase ; plasmid ; recombinant
    Source: Elsevier Journal Backfiles on ScienceDirect 1907 - 2002
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
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  • 6
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    Springer
    Journal of industrial microbiology and biotechnology 12 (1993), S. 256-262 
    ISSN: 1476-5535
    Keywords: Listeria ; Salmonella ; Shigella ; Aeromonas ; Staphylococcus ; Escherichia coli ; Bacillus cereus ; Clostridium botulinum
    Source: Springer Online Journal Archives 1860-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Summary MKES Tools is a microbial kinetics expert system for developing food production systems and assessing product safety. The specific information required as input are: (1) a flowchart of the production system, (2) the factors affecting the survival and growth of food-borne pathogens and (3) the ranges of variation for each factor's parameters. With this information, MKES Tools simulates the growth and survival of pathogenic microorganisms when subjected to many different factor/parameter situations. The responses obtained are then used to estimate the significance of each factor's parameters.
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  • 7
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    Springer
    Journal of industrial microbiology and biotechnology 14 (1995), S. 218-225 
    ISSN: 1476-5535
    Keywords: Caesium ; Potassium ; Toxicity ; Accumulation ; Escherichia coli ; Bacillus subtilis
    Source: Springer Online Journal Archives 1860-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Summary Toxicity screening ofEscherichia coli NCIB 9484 andBacillus subtilis 007, NCIB 168 and NCIB 1650 has shown Cs+ to be the most toxic Group 1 metal cation. However, toxicity and accumulation of Cs+ by the bacteria was affected by two main external factors; pH and the presence of other monovalent cations, particularly K+. Over the pH range 6–9 bothE. coli andB. subtilis showed increasing sensitivity towards caesium as the pH was raised. The presence of K+ and Na+ in the laboratory media used lowered caesium toxicity and lowered acumulation of the metal. In order to assess accurately Cs+ toxicity towards the bacterial strains it was therefore necessary to define the K+:Cs+ ratio in the external medium. The minimum inhibitory K+:Cs+ concentration ratio for theBacillus strains tested was in the range 1∶2–1∶3 whileE. coli had a minimum inhibitory K+:Cs+ concentration ratio of 1∶6.
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  • 8
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    Springer
    Journal of industrial microbiology and biotechnology 16 (1996), S. 364-369 
    ISSN: 1476-5535
    Keywords: biornass ; growth ; phosphate uptake ; Pseudomans fluorescens ; Escherichia coli ; Acinetobacter radioresistens
    Source: Springer Online Journal Archives 1860-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Abstract The ability ofPseudomonas fluorescens, Escherichia coli andAcinetobacter radioresistenns to remove phosphate during growth was related to the initial biomass as well as to growth stages and bacterial species. Phosphate was removed by these bacteria under favourable conditions as well as under unfavourable conditions of growth. Experiments showed a relationship between a high initial cell density and phosphate uptake. More phosphate was released than removed when low initial cell densities (102–105 cells ml−1) were used. At a high initial biomass concentration (108 cells ml−1), phosphate was removed during the lag phase and during logarthmic growth byP. fluorescens. Escherichia coli. at high initial biomass concentrations (107 cells ml−1), accumulated most of the phosphate during the first hour of the lag phase and/or during logarithmic growth and in some cases removed a small quantily of phosphate during the stationary growth phase.Acinetobacter radioresistens, at high initial cell densities (106, 107 cells ml−1) removed most of phosphate during the first hour of the lag phase and some phosphate during the stationary growth phase.Pseudomonas fluorescens removed phosphate more thanA. radioresistens andE. coli with specific average ranges from 3.00–28.50 mg L−1 compared to average ranges of 4.92–17.14 mg L−1 forA. radioresistens and to average ranges of 0.50–8.50 mg L−1 forE. coli.
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  • 9
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    Springer
    Journal of industrial microbiology and biotechnology 3 (1988), S. 21-28 
    ISSN: 1476-5535
    Keywords: Diaper ; Staphylococcus aureus ; Escherichia coli ; Candida albicans
    Source: Springer Online Journal Archives 1860-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Summary Methods were developed to study the effects of absorbent materials from diapers on microbial survival, growth and toxic shock syndrome toxin-1 (TSST-1) production under specified in vitro conditions. Growth of representative skin and fecal flora organisms was equivalent in cultures in which materials from cotton cloth diapers, disposable diapers or disposable diapers containing absorbent gelling material were added as the sole carbon source. In urine used as an enrichment medium, growth of the test organisms in media containing material from the three diaper types was equivalent and no contribution to growth from the diaper material was detected. TSST-1 was not produced byStaphylococcus aureus under conditions in which urine was added to the diaper materials. Pathogenic strains of organisms purposefully introduced onto diapers failed to survive and the few microbial cells normally found in diaper material did not multiply when stored under conditions favorable to microbial growth. The data indicate that all three diaper types tested were the same with respect to growth and survival of representative skin and fecal organisms.
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  • 10
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    Springer
    Journal of industrial microbiology and biotechnology 4 (1989), S. 1-5 
    ISSN: 1476-5535
    Keywords: Xylose isomerase ; Enzyme expression ; thermally inducible ; Hollow fiber bioreactor ; Escherichia coli
    Source: Springer Online Journal Archives 1860-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Summary TheEscherichia coli xylose isomerase (EC 5.3.1.5) has been expressed under the control of a thermal inverting promotor system (att-nutL-p-att-N block) and its performance in a hollow fiber bioreactor measured. The conversion of xylose to xylulose was inversely proportional to the flow rate and the system operated up to 60°C. The maximum conversion efficiency observed was 19.05% at 55°C.
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  • 11
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    Springer
    Journal of industrial microbiology and biotechnology 1 (1987), S. 335-340 
    ISSN: 1476-5535
    Keywords: Escherichia coli ; Outer membrane permeability ; Porin
    Source: Springer Online Journal Archives 1860-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Summary We describe the construction and analysis of an isogenic series ofEscherichia coli K12 strains that vary in their outer membrane permeability. They carry mutations that alter the amount and the type of porin present in the outer membrane. The permeability profiles of these strains suggest that both the amount and the type of porin present in the outer membrane affects permeability. Several of the strains carry mutations that extend the permeability of the outer membrane to include a variety of compounds that are normally excluded from entering the cell.
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  • 12
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    Springer
    Journal of industrial microbiology and biotechnology 1 (1986), S. 69-73 
    ISSN: 1476-5535
    Keywords: Escherichia coli ; Starvation ; Protein synthesis
    Source: Springer Online Journal Archives 1860-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Summary Escherichia coli bulk protein synthesis continued during the first 3–4 h of carbon starvation at 50–75% that of non-starved (growing) cells. Two-dimensional gel electrophoresis analysis of in vivo pulse-labelled proteins resolved at least 30 polypeptides with new or increased synthesis, relative to total protein synthesis, during this time. Among these polypeptides were several that were also synthesized by ethanol-treatedE. coli (heat-shock proteins). In addition, a number of unique polypeptides were synthesized by carbon-starved cells. These ‘starvation proteins’ may be involved in survival of the starving bacteria.
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  • 13
    ISSN: 1476-5535
    Keywords: Gene transfer ; Escherichia coli ; River water ; Indigenous bacteria
    Source: Springer Online Journal Archives 1860-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Summary This study examined the transfer of the plasmid pBGH1, an expression vector for bovine somatotropin (BST), fromEscherichia coli K-12 strain W3110G [pBGH1] to indigenous microorganisms present in flasks containing Missouri River water. Strain LBB269 is a nalidixic acid-resistant derivative of W3110G which was used as a plasmid-free control strain in these studies. Water samples were inoculated with strains W3110G [pBGH1] and LBB269; after 21 days of incubation the number of viable colony-forming units (CFU) of W3110G [pBGH1] and LBB269 were reduced from an initial level of about 1×107 CFU per ml to less than 1 CFU per 100 ml. At this time indigenous microbes resistant to both ampicillin and tetracycline (the antibiotic resistance markers on pBGH1) were isolated from 100 ml of water from each of the flasks inoculated with either strain W3110G [pBGH1] or LBB269. Plasmid DNA was isolated from these organisms and examined for sequences containing the gene for BST from pBGH1, using a polymerase chain reaction (PCR) assay. As expected, the day 0 sample from the flask inoculated withE. coli K-12 strain W3110G [pBGH1] gave a positive PCR response and the day 0 sample from the flask inoculated withE. coli K-12 strain LBB269 gave a negative PCR response. All of the day 21 samples containing indigenous microbes isolated from flasks that were inoculated with either W3110G [pBGH1] or LBB269 were negative in the PCR assay, indicating that the target sequence from pBGH1 was not present in any of these indigenous microorganisms. The results of this particular assay indicate that pBGH1 or the portion of pBGH1 including the BST structural gene had not been transferred from W3110G [pBGH1] to indigenous microbial inhabitants of the Missouri River water flasks during this study.
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  • 14
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    Springer
    Journal of industrial microbiology and biotechnology 16 (1996), S. 57-61 
    ISSN: 1476-5535
    Keywords: Escherichia coli ; hypochlorites ; chlorine ; inactivation kinetics
    Source: Springer Online Journal Archives 1860-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Abstract The kinetic inactivation parameters of four wild strains and two enterotoxigenic strains ofEscherichia coli exposed to commercial calcium hypochlorite were determined. The four wild strains (1A, 3C, 4D and 8H) were isolated from lettuce bought in São Paulo (Brazil), and the two enterotoxigenic strains (TR69 and TR101) were originally isolated from human patients. Decimal reduction time ‘D’, for 10 mg L−1 available chlorine at pH 6.8, varied between 71.4 s for the wild strain 4D and 31.3 s for the toxigenic strain. The ‘D’ values obtained for wild strain 1A exposed to 5.0 mg L−1 available chlorine at pH 6.8 varied between 111.1 s and 41.7 s. The ‘D’ values obtained forE. coli strain TR69 exposed to 10 mg L−1 available chlorine varied from 15.2 s at pH 5.4 up to 83.3 s at pH 8.2. The use of the most resistant wild strain ofE. coli as a biological standard assures maximal effectiveness in controlling water contamination by chlorination.
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  • 15
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    Springer
    Journal of industrial microbiology and biotechnology 17 (1996), S. 151-158 
    ISSN: 1476-5535
    Keywords: bacteriocins ; colicins ; evolution ; ecology ; Escherichia coli
    Source: Springer Online Journal Archives 1860-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Abstract In this review we focus on the ecological and evolutionary forces that determine the frequency and diversity of colicins inEscherichia coli. To begin, we describe that this killing phenotype is ubiquitous inE. coli, with as many as 50% of the isolates from a population producing colicin toxins, and that each population sampled has its own unique distribution of the more than 20 known colicin types. Next, we explore the dynamics of colicinogeny, which exhibits a typical form of frequency dependence, where the likelihood of successful colicin invasion into a population increases as the initial density of colicinogenic cells increases. We then incorporate thoughts on the evolution of chromosomal resistance to colicins and describe how resistance might influence the dynamics of colicinogen invasion and maintenance and the resulting colicin diversity. The final section deals with a genetic and phylogenetic characterization of colicins and a discussion of the evolutionary mechanisms responsible for generating colicin diversity. In this final section we provide details of the different molecular mechanisms known to play a role in generating colicin diversity, including the two most dominant forces in colincin evolution: recombination and positive, deversifying, selection.
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  • 16
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    Springer
    Journal of industrial microbiology and biotechnology 2 (1987), S. 87-95 
    ISSN: 1476-5535
    Keywords: Fermentation ; Process control ; Expression of recombinant proteins ; Escherichia coli ; Malaria vaccine
    Source: Springer Online Journal Archives 1860-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Summary A variety of feeding strategies have been described for attaining high cell densities in fed-batch fermentors. Although cell density is an important component in the produtivity of recombinant fermentations, it must be achievable with high product expression levels. Experiments were conducted to study the influence of fermentation feeding strategies on the production of a recombinant malaria antigen inEscherichia coli. C-source feeding profiles were calculated to maintain specific growth rates at 0.1, 0.2, 0.35, and 0.5 l/h prior to induction in defined and complex media using an exponential growth model. Fed-batch fermentations employing these feeding profiles effectively controlled the specific growth rates prior to induction. Antigen yields per dry cell weight did not vary with specific growth rate. Antigen yields from fed-batch fermentations achieving high cell densities were similar to batch fermentations achieving low cell densities. These results show that C-feeding policies can limit growth without reducing expression levels in some systems, and suggest applications in managing oxygen demand and catabolic by-product formation during process scale-up.
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  • 17
    ISSN: 1476-5535
    Keywords: Recombinant human insulin-like growth factor ; Escherichia coli ; Fermentation ; Production ; Somatomedin C
    Source: Springer Online Journal Archives 1860-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Summary Two kinds of fed batch fermentation processes were compared at a 10-liter scale to examine their effect on recombinant human insulin-like growth factor (IGF-1) gene expression inEscherichia coli. The difference between the two processes was the feed medium composition and whether the process used a single or dual feed during the course of the fermentation. In the dual feed system, organic nitrogen was delivered at a higher rate (50 g/h) than in the single feed system (5 g/h). The dual feed process resulted in a significant increase in IGF-1 yield. 30 mg IGF-1/g dry cell weight was synthesized in the dual feed system compared to 3 mg IGF-1/g dry cell weight obtained in the single feed system. The presence of high levels of organic nitrogen during the induction period may enhance IGF-1 synthesis by protecting the IGF-1 from proteolytic degradation. The IGF-1 yield decreased to 17 mg/g dry cell weight when the glucose supply was decreased from 17 g/h to 8 g/h during the induction period; however, an increase in glucose supply from 17 g/h to 50 g/h during the induction period did not enhance the IGF-1 synthesis. Thus, the enhancement of IGF-1 gene expression in the dual feed process was mainly dependent on a high level of organic nitrogen and an appropriate level of glucose in the medium during the induction period.
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  • 18
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    Journal of industrial microbiology and biotechnology 1 (1987), S. 377-381 
    ISSN: 1476-5535
    Keywords: Antimicrobial ; Metal salt ; Lanthanum ; Escherichia coli ; Staphylococcus aureus
    Source: Springer Online Journal Archives 1860-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Summary Rare earth metal cations are antibacterially synergistic with anionic surfactants, yielding mixtures that have bactericidal activity against a variety of gram-positive and gram-negative bacteria at minimum concentrations ranging from 16 to 125 μg/ml. Uptake of surfactant byEscherichia coli increases in the presence of lanthanum, suggesting that the role of rare earth metal cations is to reduce the net negative surface charge on the bacteria, thereby increasing the affinity between the negatively charged surfactant and the bacterial surface.
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  • 19
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    Journal of industrial microbiology and biotechnology 11 (1993), S. 253-257 
    ISSN: 1476-5535
    Keywords: Colonization ; Escherichia coli ; Gastrointestinal ; Environmental ; Survival
    Source: Springer Online Journal Archives 1860-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Summary The colonizing potential ofEscherichia coli K12 containing a vector coding for somidobove (bovine somatotropin) was determined. Treated male and female Fischer-344 rats were given a single oral gavage inoculum of sucrose with/without tetracycline (15 μg/ml). Untreated control animals received similar drinking water regimes. All animals survived until termination. There were no clinical signs of toxicity observed and no treatment-related effect upon body weight, food consumption, or efficiency of food utilization. Fresh fecal samples were collected from each rat every 24 h following inoculation and the population of the marked strain was quantitated until no bacterial colonies were observed for two consecutive days. While all inoculated rats were positive at 24 h, by 72 and 96 h all had become negative for the test (marked) strain, as were the corresponding control group throughout the test. The frozen stock of the marked strain used as the positive control demonstrated that the agar plates were selective for the test strain. Fourteen days following inoculation, all groups of rats were killed and the gastrointestinal tracts removed and treated to recover the marked strain. There was no evidence of the marked strain in the gastrointestinal tract of any rat from any group. Thus, theE. coli K12 host/vector system used in this experiment does not colonize the gastrointestinal tract of Fischer-344 rats.
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  • 20
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    Journal of industrial microbiology and biotechnology 16 (1996), S. 331-341 
    ISSN: 1476-5535
    Keywords: biofilms ; bacteriophages T4 and E79 ; Escherichia coli ; Pseudomonas aeruginosa ; SCLM ; fluorescence
    Source: Springer Online Journal Archives 1860-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Abstract Phages T4 and E79 were fluorescently-labeled with rhodamine isothiocyanate (RITC), fluoroscein isothiccyanate (FITC), and by the addition of 4′6-diamidino-2-phenylindole (DAPI) to phage-infected host cells ofEscherichia coli andPseudomonas aeruginosa. Comparisons of electron micrographs with scanning confocal laser microscope (SCLM) images indicated that single RITC-labeled phage particles could be visualized. Biofilms of each bacterium were infected by labeled phage. SCLM and epifluorescence microscopy were used to observe adsorption of phage to single-layer surface-attached bacteria and thicker biofilms. The spread of the recombinant T4 phage, YZA1 (containing an rll-LacZ fusion), within alac E. coli biofilm could be detected in the presence of chromogenic and fluorogenic homologs of galactose. Infected cells exhibited blue pigmentation and fluorescence from the cleavage products produced by the phage-encoded β-galactosidase activity. Fluorescent antibodies were used to detect nonlabeled progeny phage. Phage T4 infected both surface-attached and surface-associatedE. coli while phage E79 adsorbed toP. aeruginosa cells on the surface of the biofilm, but access to cells deep in biofilms was somewhat restricted. Temperature and nutrient concentration did not affect susceptibility to phage infection, but lower temperature and low nutrients extended the time-to-lysis and slowed the spread of infection within the biofilm.
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  • 21
    ISSN: 1476-5535
    Keywords: fermentation ; fermentation monitoring ; fermentation control ; fermentation software ; Escherichia coli
    Source: Springer Online Journal Archives 1860-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Abstract The advent of inexpensive computers and associated control and data acquisition software makes possible the development of sophisticated, configurable, integrated monitoring and control systems for small-scale laboratory and pilot-scale fermentors at low cost. We describe here the implementation of such a system, the interfacing of off-line instruments to enhance real time data analysis, low level process control and several substrate feeding protocols.
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  • 22
    ISSN: 1476-5535
    Keywords: Fermentation ; High cell density ; Escherichia coli ; RecombinantE. coli ; Atrial natriuretic factor (ANF) ; Fusion protein expression
    Source: Springer Online Journal Archives 1860-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Summary Studies are presented on the fermentation of recombinantEscherichia coli that express rat atrial natriuretic factor (ANF) as a fusion protein. Our objective was to achieve high cell density while maintaining ANF expression at the same level as observed in shake flasks. Improved fermentation conditions included: maintaining glucose concentrations at 1 g/l, using an enriched medium, adding concentrates of medium throughout the fermentation, and blending oxygen for adequate aeration. Cell densities of 12 g/l (dry weight) were achieved, which represented a 10-fold increase over non-improved conditions, while maintaining ANF levels at 7 mg/g of dry cell mass. When galactose was used as an initial carbon source or as a feed supplement, there was a 2-3-fold increase in the expression of ANF from these high-cell-density fermentations. The recombinant ANF was biologically active.
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  • 23
    ISSN: 1573-0972
    Keywords: Escherichia coli ; plasmids ; verotoxin
    Source: Springer Online Journal Archives 1860-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Abstract Three strains of verotoxin-producing Escherichia coli isolated from patients with haemorrhagic colitis harboured plasmids ranging in size from 2.7 kb to 91.2 kb. Those plasmids ranging from 2.7 kb to 6.8 kb hybridized to Shiga-like toxin I and Shiga-like toxin II gene probes.
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  • 24
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    World journal of microbiology and biotechnology 12 (1996), S. 585-588 
    ISSN: 1573-0972
    Keywords: Aerobactin ; colicin ; Escherichia coli ; growth ; plasmid profile
    Source: Springer Online Journal Archives 1860-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Abstract Plasmids were detected in 31 out of 35 strains of Escherichia coli isolated from unclassified cases of urinary tract infection at a median value of 1.88 plasmid bands per isolate. The isolates showed an association of aerobactin and colicin production with the distribution of plasmid bands having a median value of 2.33 and 1.72 (plasmid bands per isolate) in aerobactin-positive and aerobactin-negative strains respectively. For colicin producers, the median plasmid bands per isolate was 3.66 compared to 1.80 for colicin-negative strains.
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  • 25
    ISSN: 1573-0972
    Keywords: Escherichia coli ; diamines ; homospermidine synthase ; polyamines ; spermidine deficiency ; spermidine synthase
    Source: Springer Online Journal Archives 1860-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Abstract The Escherichia coli mutant speE deficient in the gene encoding for spermidine synthase has no absolute requirement for spermidine but shows a retarded growth rate. This growth retardation could be unspecifically restored to the respective wild type level by exogenously supplied polyamines such as spermidine, spermine and homospermidine as well as the diamines putrescine and cadaverine. In comparison to the respective wild type, the mutant shows a two-fold increased level of endogenous putrescine but displays a reduced ability to accumulate the diamines putrescine and cadaverine. The ability to accumulate polyamines is not affected. The deleted spermidine synthase gene of the mutant was substituted by heterologous expression of the hss gene from Rhodopseudomonas viridis encoding homospermidine synthase.
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  • 26
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    World journal of microbiology and biotechnology 15 (1999), S. 65-71 
    ISSN: 1573-0972
    Keywords: Escherichia coli ; fedbatch cultivation ; growth rate ; high cell density ; plasmid stability
    Source: Springer Online Journal Archives 1860-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Abstract The effect of higher cell densities on the expression and segregational stability of a recombinant E. coli- B. subtilisshuttle plasmid coding for carboxymethylcellulase (CMCase) activity, was studied in E. coli DH5α. Of the various feeding policies adopted for maximal expression and stability, exponential feeding resulted in the highest biomass of 15g dry cell weight (DCW) l−1 and plasmid stability of 45%. A CMCase activity of 11400 Uml−1 was achieved as compared to 230 Uml−1 during batch cultivation. In the case of other feeding strategies viz., constant feeding, linear feeding or intermittent feeding, the plasmid stability varied between 20% to 60%. Biomass achieved ranged from 5.0 g DCW l−1 to 9.0 g DCW l−1 and enzyme activities were between 2550 Uml−1 and 6000 Uml−1.
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  • 27
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    World journal of microbiology and biotechnology 15 (1999), S. 497-499 
    ISSN: 1573-0972
    Keywords: Amylose ; amylopectin ; Escherichia coli ; β-glucuronidase ; pullulan ; starch
    Source: Springer Online Journal Archives 1860-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Abstract Synthesis of β-glucuronidase in starch-degrading Escherichia coli (S1) was induced by amylose, amylopectin and pullulan supplied in mineral medium as the sole carbon source (1%, w/v). The maximum activity occurred after 4 days when cultures reached the stationary phase of growth, but induction was also evident during log-phase. The effects obtained with amylose, amylopectin and pullulan were higher than that obtained with maize starch.
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  • 28
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    World journal of microbiology and biotechnology 16 (2000), S. 719-724 
    ISSN: 1573-0972
    Keywords: Escherichia coli ; haemolytic uraemic syndrome ; haemorrhagic colitis ; pathogenicity ; Verocytotoxin ; VTEC
    Source: Springer Online Journal Archives 1860-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Abstract In 1977, Konowalchuk and colleagues (Konowalchuk, J., Speirs, J.I. & Stavric, S. 1977 Infection and Immunity 18, 775–779) were the first to describe Verocytotoxin-producing strains of Escherichia coli or VTEC. The surveillance of infection caused by VTEC demonstrated strains of E. coli belonging to serogroup O157 as the main cause of human infection capable of causing haemorrhagic colitis (HC) and haemolytic uraemic syndrome (HUS). Infection with O157 VTEC results in a range of disease manifestations including abdominal cramps, vomiting and fever. This frequently leads to cases with bloody diarrhoea and HC, and approximately 10% of patients develop HUS. The symptoms of disease caused by VTEC O157 have been well documented and the pathogenic mechanisms expressed by VTEC have been the focus of considerable attention. However, the role of putative pathogenic mechanisms in the pathogenesis of disease is not fully understood. The aim of this review is to consider the clinical aspects of infection with strains of VT-producing E. coli O157 in terms of the putative pathogenic mechanisms expressed by these bacteria.
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  • 29
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    World journal of microbiology and biotechnology 9 (1993), S. 609-610 
    ISSN: 1573-0972
    Keywords: Antibiotics ; Escherichia coli ; resistance ; river water
    Source: Springer Online Journal Archives 1860-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Abstract Of 107 Escherichia coli strains isolated from the water, sediment and fish of the Bhavani River, all of which are considered potential causes of human enteric disease, 62% were resistant to more than four antibiotics. Levels of resistance to bacitracin, penicillin, and novobiocin were generally high whereas those to polymyxin-B and chloramphenicol were much lower. A high incidence of multiple antibiotic resistant E. coli was noted in all samples and the multiple antibiotic resistance index of the strains showed that 95% of the strains originated either from man or cattle.
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  • 30
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    World journal of microbiology and biotechnology 13 (1997), S. 619-625 
    ISSN: 1573-0972
    Keywords: Alcohol ; biofuel ; corn fibre ; corn germ ; Escherichia coli ; fermentation
    Source: Springer Online Journal Archives 1860-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Abstract Corn hulls and corn germ meal were both evaluated as feedstocks for production of ethanol for biofuel. Currently, these fibrous co-products are combined with corn steep liquor and the fermentation bottoms (if available) and marketed as cattle feed. Samples were obtained from wet and dry corn mills. The corn hulls and germ meal were evaluated for starch and hemicellulose compositions. Starch contents were 12 to 32% w/w and hemicellulose (arabinoxylans) contents were 23 to 64% w/w. Corn fibrous samples were hydrolysed, using dilute sulphuric acid, into mixed sugar streams containing arabinose, glucose and xylose. Total sugar concentrations in the hydrolysate varied from 8.4 to 10.8% w/v. The hydrolysates were fermented to ethanol using recombinant E. coli strains K011 and SL40. Ethanol yields were 0.38 to 0.41g ethanol produced/g total sugars consumed and fermentations were completed in 60h or less. However, residual xylose was detected for each hydrolysate fermentation and was especially significant for fermentations using strain SL40. Strain K011 was a superior ethanologenic strain compared with strain SL40 in terms of both ethanol yield and maximum productivity.
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  • 31
    ISSN: 1573-0972
    Keywords: Acetic acid production ; carbon metabolism ; continuous culture ; Escherichia coli ; metabolic engineering
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    Notes: Abstract The growth kinetics of an Escherichia coli wild type strain and two derivative mutants were examined in batch cultures and in glucose-limited chemostats. One mutant (PB12) had an inactive phosphotranferase transport system and the other (PB25) had interrupted pykA and pykF genes that code for the two pyruvate kinase isoenzymes. In both batch and continuous culture, important differences in acetic acid accumulation and other metabolic activities were found. Compared to the wild type strain, we observed a reduction in acetic acid accumulation of 25 and 80% in PB25 and PB12 strains respectively, in batch culture. Continuous culture experiments revealed that compared to the other two strains, PB25 accumulated less acetic acid as a function of dilution rate. In continuous cultures, oxidoreductase metabolic activities were substantially affected in the two mutant strains. These changes in turn were reflected in different levels of biomass and CO2 production, and in oxygen consumption.
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  • 32
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    World journal of microbiology and biotechnology 13 (1997), S. 159-161 
    ISSN: 1573-0972
    Keywords: Escherichia coli ; plasmid-containing bacteria ; pond water ; survival
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    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Abstract The survival of Escherichia coli K-12 J62-1 containing the antibiotic-resistance plasmid R1 and an isogenic plasmid-free strain were studied in pond water microcosms. The number of plasmid-containing cells recovered from the microcosms remained constant over a sampling period of 31 days whereas plasmid-free cell numbers declined.
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  • 33
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    World journal of microbiology and biotechnology 9 (1993), S. 34-36 
    ISSN: 1573-0972
    Keywords: Bacteriophages ; Escherichia coli ; Salmonella ; sewage ; wastewater
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    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Abstract A new method for quantifying F-specific bacteriophages in wastewater is described. Somatic coliphages were also determined. Host-strainSalmonella typhimurium WG 49 was sensitive to only a few bacteriophages and this could have arisen from infection by F-RNA phages. Host-strainEscherichia coli ATCC 9723 C, however, supported multiplication of a wide range of bacteriophages present in sewage, giving plaque counts one to three orders of magnitude greater than those on F+ and F- salmonellas.
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  • 34
    ISSN: 1573-0972
    Keywords: Bacterial adherence ; bromodeoxyuridine (BrdU) ; Escherichia coli ; fimbria ; immunomax technique
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    Notes: Abstract Fimbriated and fimbria-less strains of Escherichia coli were isolated from urine of pyelonephritis patients, labelled with bromodeoxyuridine and their adhesion to human umbillical vein endothelial cells was studied employing ELISA and immunocytochemistry. No significant differences were noted in adhesion of the two types of strains.
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  • 35
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    World journal of microbiology and biotechnology 15 (1999), S. 475-480 
    ISSN: 1573-0972
    Keywords: α-Amylase ; Bacillus laterosporus ; cloning ; Escherichia coli ; secretion
    Source: Springer Online Journal Archives 1860-2000
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    Notes: Abstract α-Amylase gene from Bacillus laterosporus P3 was cloned and expressed in Escherichia coli HB101 and DH5α. Up to 92% of the cloned gene product was secreted into the medium by the recombinant E. coli. The recombinant crude enzyme showed improved functionality in terms of activity at a wider pH range and at higher temperature, as compared to the crude enzyme from the donor strain. The improved functionality of the cloned enzyme was due to the absence of a contaminating protease which was co-produced in the donor strain. Sub-cloning of the α-amylase gene using the promoter-probe vector, pKT240 in E. coli DH5α indicated the presence of a promoter of B. laterosporus P3 in the cloned fragment.
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  • 36
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    World journal of microbiology and biotechnology 14 (1997), S. 263-269 
    ISSN: 1573-0972
    Keywords: Escherichia coli ; fluorescence ; NAD(P)H ; nitrate reduction ; nitrite reduction
    Source: Springer Online Journal Archives 1860-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Abstract When nitrate was added to anaerobic resting cultures of Escherichia coli, two different profiles of NAD(P)H fluorescence were observed. E. coli is known to reduce nitrate to ammonia via nitrite as an anaerobic respiration mechanism. The profile showing single-stage response corresponded to situations where the nitrite formed from nitrate reduction was immediately converted to ammonia. The other profile showing two-stage response resulted from a much slower reduction of nitrite than nitrate. Nitrite thus accumulated during the first stage and was gradually reduced to ammonia when nitrate was depleted, i.e. in the second stage. An undamped oscillation of NAD(P)H fluorescence was also observed in the cultures showing the two-stage response. The oscillation was always detected during the second stage and seldom during either the first stage or the recovered anaerobic stage (after complete nitrite reduction). It never occurred in the cultures showing the single-stage response. The period of oscillation ranged from 1 to 5min. The possibility of the common glycolytic oscillation being responsible is low, as judged from the current knowledge of the nitrate/nitrite reductases of E. coli and the observations in this study. This is the first report on the occurrence of oscillatory NAD(P)H fluorescence in E. coli.
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  • 37
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    World journal of microbiology and biotechnology 10 (1994), S. 346-347 
    ISSN: 1573-0972
    Keywords: Chromatography ; Escherichia coli ; plasmid ; transfection
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    Notes: Abstract A simple procedure to obtain plasmid preparations, suitable for transfecting mammalian cell lines using a calcium phosphate co-precipitation technique, is described. The protocol is based on the purification of plasmid DNA by double gel-filtration chromatography on Sephacryl S-1000 and additional slight modifications to the original transfection procedure. The purity of plasmid preparation was verified by analytical methods. The resulting preparation efficiently transfected NIH-3T3 cells.
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  • 38
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    Biotechnology and Bioengineering 55 (1997), S. 556-564 
    ISSN: 0006-3592
    Keywords: cumulative sedimentation analysis ; cell debris size ; Escherichia coli ; homogenization ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
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    Notes: A new method to measure Escherichia coli cell debris size after homogenization is presented. It is based on cumulative sedimentation analysis under centrifugal force, coupled with Sodium Dodecyl Sulfate-Polyacrylamide Gel Electrophoresis (SDS-PAGE) analysis of sedimented proteins. The effects that fermentation and homogenization conditions have on the resulting debris distributions were investigated using this method. Median debris size decreased significantly from approximately 0.5 μm to 0.3 μm as the number of homogenization passes increased from 2 to 10. Under identical homogenization conditions, uninduced host cells in stationary phase had a larger debris size than exponential cells after 5 homogenizer passes. This difference was not evident after 2 or 10 passes, possibly because of confounding intact cells and the existence of a minimum debris size for the conditions investigated. Recombinant cells containing protein inclusion bodies had the smallest debris size following homogenization. The method was also used to measure the size distribution of inclusion bodies. This result compared extremely well with an independent determination using centrifugal disc photosedimentation (CDS), thus validating the method. This is the first method that provides accurate size distributions of E. coli debris without the need for sample pretreatment, theoretical approximations (e.g. extinction coefficients), or the separation of debris and inclusion bodies prior to analysis. © 1997 John Wiley & Sons, Inc. Biotechnol Bioang 55: 556-564, 1997.
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  • 39
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    Biotechnology and Bioengineering 57 (1998), S. 228-237 
    ISSN: 0006-3592
    Keywords: AlkB ; Pseudomonas oleovorans ; alkane hydroxylase ; iron ; Escherichia coli ; alk + recombinants ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: The alk genes enable Pseudomonas oleovorans to utilize alkanes as sole carbon and energy source. Expression of the alk genes in P. oleovorans and in two Escherichia coli recombinants induced iron limitation in minimal medium cultures. Further investigation showed that the expression of the alkB gene, encoding the integral cytoplasmic membrane protein AlkB, was responsible for the increase of the iron requirement of E. coli W3110 (pGEc47).AlkB is the non-heme iron monooxygenase component of the alkane hydroxylase system, and can be synthesized to levels up to 10% (w/w) of total cell protein in E. coli W3110 (pGEc47). Its synthesis is, however, strictly dependent on the presence of sufficient iron in the medium. Our results show that a glucose-grown E. coli alk+ strain can reach alkane hydroxylase activities of about 25 U/g cdw, and are consistent with the recent finding that catalytically active AlkB contains two, rather than one iron atom per polypeptide chain. © 1998 John Wiley & Sons, Inc. Biotechnol Bioeng 57: 228-237, 1998.
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  • 40
    ISSN: 0006-3592
    Keywords: Escherichia coli ; acetate ; protein, recombinant ; Chemistry ; Biochemistry and Biotechnology
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    Notes: Two Escherichia coli strains, widely used for the production of various recombinant proteins, were compared for their pre-induction growth and acetate accumulation patterns. The strains studied were E. coli BL21 (λDE3), transformed with a plasmid encoding Pseudomonas exotoxin A, and an E. coli K12 derived strain, JM109, carrying a plasmid encoding maltose-binding protein fused with HIV protease. Cultures were grown in controlled bench-top fermentors to the optimal pre-induction density in both high glucose batch and low glucose fed batch strategies. The results showed the superiority of E. coli BL21 (λDE3) as a host for a recombinant protein expression system. For example, JM109 responds differently to high glucose concentration and to low glucose concentration. Its acetate concentration was as high as 10 g/L in a batch mode and 5 g/L in a fed batch mode. In comparison, strain BL21 (λDE3) reached 2 g/L acetate when grown in batch mode and not more than 1 g/L acetate when grown in a fed batch mode. E. coli BL21 (λDE3), most likely, possesses an acetate self-control mechanism which makes it possible to grow to the desired pre-induction density in a high glucose medium using simple batch propagation techniques. Such a technique is cost effective, reproducible, and easy to scale up. © 1996 John Wiley & Sons, Inc.
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  • 41
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    Biotechnology and Bioengineering 51 (1996), S. 15-22 
    ISSN: 0006-3592
    Keywords: preparative separation ; continuous ; free-flow zone electrophoresis ; electrophoretic mobility ; net charge ; enzymes ; proteins ; crude extract ; cell debris ; Candida boidinii ; Escherichia coli ; formate dehydrogenase ; formaldehyde dehydrogenase ; methanol oxidase ; β-galactosidase ; Chemistry ; Biochemistry and Biotechnology
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    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Continuous, single-step, state-of-the-art preparative separations of enzymes from microorganism crude extracts by free-flow zone electrophoresis are presented. In the first example, the enzymes formate dehydrogenase, formaldehyde dehydrogenase, and methanol oxidase were continuously separated from Candida boidinii crude extract. Yields of 85% to 95% and purification factors between 3 and 7 were obtained along with a simultaneous separation of the finer cell debris from the enzymes. Using multiple injections of sample, a throughput of 46.2 mg protein/h was recorded. In the second example, a fivefold purification of β-galactosidase from Escherichia coli was achieved along with complete, simultaneous cell debris separation from the enzyme. The yield of the enzyme was greater than 90%. The preparative free-flow zone electrophoresis experiments were run continuously for a period of 12 h and the separations were found to be stable; i.e., the enzymes and the cell debris eluted at their respective fraction numbers during the entire period. In both examples, choice of the type of buffer played a critical role and had to be investigated and optimized experimentally. Scale-up aspects of the separations are also discussed. Recently, by comparison of free-flow zone electrophoresis with ion-exchange chromatography, we have presented evidence that free-flow electrophoresis separations are governed by net surface charge (S. Nath et al., Biotechnol. Bioeng. 1993, 42: 829-835). Here, we offer further confirmation of this evidence by comparison of preparative free-flow zone electrophoresis experiments at various pHs on a mixture of two model proteins with analytical electrophoretic titration curves of the proteins. We are thus in a position to predict separations in free-flow zone electrophoresis. © 1996 John Wiley & Sons, Inc.
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  • 42
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    Biotechnology and Bioengineering 51 (1996), S. 720-724 
    ISSN: 0006-3592
    Keywords: hybrid protein ; dielectric permeability ; electroconductivity ; electro-optical properties ; Escherichia coli ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: A novel method for monitoring the cell culture process has been developed. The method is based on the measurements of electro-optical characteristics of cell suspension, calculation of cell structure parameters, and the relationship between accumulation of proteins and change of these parameters' employment. Application of the method for the monitoring of a culture process of a recombinant strain is considered. The process of growth of recombinant strains cannot be sufficiently predicted and the direct measurement of cell culture parameters is unlikely to be the most efficient way of solving the problem.Escherichia coli plasmid-free and recombinant strains synthesizing the fusion protein consisting of tumor necrosis factor-α (TNF) and thymosin-α1 (T) were studied. It was found that cytoplasmic electroconductivity of the strains investigated increased during the culture process. The accumulation of insoluble recombinant pThy-315-encoded hybrid protein TNF(SINGLEBOND)T in cells resulted in a decrease of the membrane dielectric permeability. To determine variations of membrane dielectric permeability the amount of insoluble recombinant protein TNF(SINGLEBOND)T in the bacterial cells should be calculated.
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  • 43
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    Biotechnology and Bioengineering 52 (1996), S. 129-140 
    ISSN: 0006-3592
    Keywords: pathway engineering ; central metabolism ; phosphoenolpyruvate synthase ; phosphoenolpyruvate carboxykinase ; aromatic amino acid ; Escherichia coli ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: The rate and yield of producing a metabolite is ultimately limited by the ability to channel metabolic fluxes from central metabolism to the desired biosynthesis pathway. Redirection of central metabolism thus is essential to high-efficiency production of biochemicals. This task begins with pathway analysis, which considers only the stoichiometry of the reaction networks but not the regulatory mechanisms. An approach extended from convex analysis is used to determine the basic reaction modes, which allows the determination of optimal and suboptimal flux distributions, yield, and the dispensable sets of reactions. Genes responsible for reactions in the same dispensable set can be deleted simultaneously. This analysis serves as an initial guideline for pathway engineering. Using this analysis, we successfully constructed an Escherichia coli strain that can channel the metabolic flow from carbohydrate to the aromatic pathway with theoretical yield. This analysis also predicts a novel cycle involving phosphoenolpyruvate (PEP) carboxykinase (Pck) and the glyoxylate shunt, which can substitute the tricarboxylic acid cycle with only slightly less efficiency. However, the full cycle could not be confirmed in vivo, possibly because of the regulatory mechanism not considered in the pathway analysis.In addition to the kinetic regulation, we have obtained evidence suggesting that central metabolites are involved in specific regulons in E. coli. Overexpression of PEP-forming enzymes (phosphoenolpyruvate synthase [Pps] and Pck) stimulates the glucose consumption rate, represses the heat shock response, and negatively regulates the Ntr regulon. These results suggest that some glycolytic intermediates may serve as a signal in the regulation of the phosphotransferase system, heat shock response, and nitrogen regulation. However, the role of central metabolites in these regulations has not been determined conclusively. © 1996 John Wiley & Sons, Inc.
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  • 44
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    Biotechnology and Bioengineering 52 (1996), S. 340-356 
    ISSN: 0006-3592
    Keywords: laser microscopy, confocal scanning ; Escherichia coli ; biofilms ; immobilization ; confocal scanning laser microscopy ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Properties of a novel, synthetic biofilm were examined by using confocal scanning laser microscopy (CSLM) in combination with fluorescent probes and by investigating total protein content and specific β-galactosidase activity during various steps of the biofilm preparation. Viable, but nongrowing Escherichia coli were entrapped in 10- to 80-μm-thick multilayer films, where a copolymer of acrylic and vinyl acetate was the immobilization matrix. Cell viability and distribution within the films were evaluated by developing a protocol to stain the bacteria with fluorescein isothiocyanate and propidium iodide, thereby labeling all cells green and dead cells red, respectively. Confocal microscopy facilitated viewing samples in the XY and XZ planes, and image analysis enabled counting of the cells. These experiments showed that the initial viability of the entrapped bacteria was 85% to 90%, cell distribution was uniform in the XY plane and cell number increased with increasing depth into the film. Specific β-galactosidase assays developed here allowed comparison of the induction of lacZin suspended and immobilized cells. These experiments demonstrated that rehydration was an important step in biofilm preparation, and E. coli cast into synthetic biofilms with cell layers of at least 20 to 35 μm in thickness had gene induction characteristics similar to suspended cells. © 1996 John Wiley & Sons, Inc.
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  • 45
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    Biotechnology and Bioengineering 52 (1996), S. 271-289 
    ISSN: 0006-3592
    Keywords: bioprocess control ; physiological state ; Escherichia coli ; plant cell culture ; mammalian cell culture perfusion ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Advances in bioprocess engineering depends ultimately on the level of understanding and control of the physiological state of the cell population. Process efficiency is strongly influenced by changes in the cellular state which should be monitored, interpreted, and, if possible, properly manipulated. In most control systems this function is not explicitly considered, which hampers process development and optimization. Conventional control logic is based on direct mapping of the growth environment into process efficiency, thereby bypassing the cell state as an intermediate control objective. Today, this limitation is well realized, and explicit monitoring and control of cellular physiology are considered to be among the most challenging tasks of modern bioprocess engineering. We present here a generic methodology for the design of systems capable of performing these advanced monitoring and control functions.The term “physiological state” is quantified by a vector composed of several process variables that convey significant information about cellular state. These variables can be selected among different classes, including specific metabolic rates, metabolic rate ratios, degees of limitation, and others. The real-time monitoring of many of these is possible using commercial sensors. The definition and calculation of representative sets of physiological state variables is demonstrated with examples from several fermentor cultures: recombinant Escherichia coli for phenylalanine production, bioluminescent E. coli (harboring lux genes driven by a heat shock protein promoter) for detection of environmental pollutants, plant cell culture of Perilla frutescensfor anthocyanin production, and perfusion cultures of recombinant mammalian cells (NS0 and CHO) for therapeutic protein production.If the physiological state vector is on-line calculated, the fermentation process can be described by its trajectory in a space defined by the vector components. Then, the goal of the control system is to maintain the physiological state of the cell as close as possible to the trajectory, providing maximum efficiency. A control structure meant to perform this function is proposed, along with the mechanism for its design. In contrast to conventional systems which work in a closed loop in respect to the cell environment, this scheme operates in a closed loop in respect to the cell state. The discussed control concept has been successfully applied to the recombinant phenylalanine production, resulting in physiologically consistent operation, total computer control, and high process efficiency. Initial results from the application of the method to perfusion mammalian cell cultures are also presented. © 1996 John Wiley & Sons, Inc.
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  • 46
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    Biotechnology and Bioengineering 52 (1996), S. 572-578 
    ISSN: 0006-3592
    Keywords: nar promoter ; inducible promoter ; nitrate reductase ; anaerobic conditions ; Escherichia coli ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: The nar promoter of Escherichia coli, which is maximally induced under anaerobic conditions in the presence of nitrate, was characterized to see whether the nar promoter cloned onto pBR322 can be used as an inducible promoter. To increase the expression level, the nar promoter was expressed in E. coli where active nitrate reductase cannot be expressed from the nar operon on the chromosome. A plasmid with the lacZ gene expressing β-galactosidase instead of the structural genes of the nar operon was used to simplify an assay of induction of the nar promoter. The following effects were investigated to find optimal conditions: methods of inducing the nar promoter, optimal nitrate and molybdate concentrations maximally inducing the nar promoter, the amount of expressed β-galactosidase, and induction ratio (specific β-galactosidase activity after maximal induction/specific β-galactosidase activity before induction.)The following results were obtained from the experiments: induction of the nar promoter was optimal when E. coli was grown in the presence of 1% nitrate at the beginning of culture; expression of β-galactosidase was not affected by molybdate; the induction ratio was maximal, approximately 300, when the overnight culture was grown in the flask for 2.5 h (OD600 is congruent to 1.3) before being transferred to the fermentor; the amount of β-galactosidase per cell and per medium volume was maximal when E. coli was grown under aerobic conditions to OD600 = 1.7; then the nar promoter was induced under microaerobic conditions made by lowering dissolved oxygen level (DO) to 1-2%. After approximately 6 h of induction, OD600 became 3.2 and specific β-galactosidase activity became 36,000 Miller units, equivalent to 35% of total cellular proteins, which was confirmed from sodium dodecyl sulfate-polyacrylamide gel electrophoresis. © 1996 John Wiley & Sons, Inc.
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  • 47
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    Biotechnology and Bioengineering 52 (1996), S. 615-624 
    ISSN: 0006-3592
    Keywords: Escherichia coli ; ribosome synthesis ; functioning ribosome ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: The effect of temperature on the synthesis of ribosome in Escherichia coli K-12 was investigated. In continuous fermentation, the total and functioning ribosome contents decreased with increasing temperature, while the non-functioning ribosome content remained unchanged. Cells contained higher amounts of functioning ribosome at lower temperatures to compensate for the decrease in translational activity. A transient study was performed to investigate the dynamic response of the cell to changes in the dilution rate. In response to the dilution rate shift-up, the cell mass decreased until the cells produced a sufficient amount of ribosomes to support the new higher growth rate. However, the response to the dilution rate shift-down resulted in an immediate increase in cell mass. This may be due to the fact that the cell already contains enough ribosomes to support a lower growth rate corresponding to the new low dilution rate. Based on the experimental results, a mathematical model was developed to describe the cell growth at transient as well as steady states. The total ribosome content was included as a variable because it affects the growth rate of the cell. © 1996 John Wiley & Sons, Inc.
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  • 48
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    Keywords: poly(3-hydroxybutyrate) ; Escherichia coli ; PHB synthesis ; regulation ; nicotinamide nucleotides ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Regulatory roles of nicotinamide nucleotides and three key enzymes, β-ketothiolase (KT), NADPH-dependent acetoacetyl-CoA reductase (AAR), and citrate synthase (CS), on poly(3-hydroxybutyrate) (PHB) synthesis in recombinant Escherichia coli harboring a plasmid containing the Alcaligenes eutrophus polyhydroxyalkanoate (PHA) biosynthesis genes were examined. Cells were grown in various media and were subsequently compared for PHB concentration, PHB content, the activities of the key enzymes, and the levels of nicotinamide nucleotides. Cells of recombinant E. coli accumulated the largest amount of PHB in LB+glucose medium among those tested. PHB synthesis was not enhanced by limiting inorganic ions. The activity of CS, which competes with KT for acetyl-CoA, was lower when cells were grown in LB+glucose compared with other media. The NADPH level and the NADPH/NADP ratio were high in LB+glucose. Examination of the time profiles of the specific PHB synthesis rate, key enzyme activities, and the levels of nicotinamide nucleotides showed that PHB synthesis is most significantly affected by the NADPH level. Even though the NADH level and the NADH/NAD ratio were also high during the synthesis of PHB, no direct evidence of their positive effect on PHB synthesis was found. Low activity of CS was beneficial for PHB synthesis due to the availability of more acetyl-CoA to PHB biosynthetic pathway. In recombinant E. coli, the level of NADPH and/or the NADPH/NADP ratio seem to be the most critical factor regulating the activity of AAR and, subsequently, PHB synthesis. © 1996 John Wiley & Sons, Inc.
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  • 49
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    Biotechnology and Bioengineering 53 (1997), S. 238-241 
    ISSN: 0006-3592
    Keywords: Escherichia coli ; bacterial motility ; geometrical restriction ; capillary tube ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Motility of Escherichia coli K-12 cells was studied in a capillary tube with an inside diameter of 3 μm, which is comparable to the size of the cells' body. The extreme restriction, imposed by the capillary on the bacterial motility, caused a series of phenomena such as cell aggregation, swimming as a cluster, and break-up of aggregates, which were observable for the first time, and which are reported here. © 1997 John Wiley & Sons, Inc.
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    Biotechnology and Bioengineering 53 (1997), S. 379-386 
    ISSN: 0006-3592
    Keywords: ppGpp ; recombinant protein synthesis ; translational machinery ; Escherichia coli ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Maintaining a metabolically productive state for recombinant Escherichia coli remains a central problem for a wide variety of growth-dependent biosynthesis. This problem becomes particularly acute under conditions of minimal cell growth such as fed-batch fermentations. In this, we investigated the possibility of manipulating the protein synthesis machinery of E. coli whereby synthesis of foreign proteins might be decoupled from cell growth. In particular, the effects of eliminating intracellular ppGpp on the synthesis of foreign proteins were studied in both batch and fed-batch operations. A significant increase in CAT production was observed from the ppGpp-deficient strain during both exponential and fed-batch phases. The increase in CAT production during exponential growth was accompanied by a simultaneous increase in CAT mRNA levels. Interestingly, CAT production was increased five-fold, while the level of CAT-specific mRNA increased only three-fold. Thus, eliminating intracellular ppGpp appears to have increase the production of recombinant protein by increasing not only the pool sizes of CAT mRNA but also possible alternations in the post-transcriptional processes. © 1997 John Wiley & Sons, Inc. Biotechnol Bioeng 53: 379-386, 1997.
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  • 51
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    Biotechnology and Bioengineering 53 (1997), S. 453-458 
    ISSN: 0006-3592
    Keywords: chemical permeabilization ; cell disruption ; urea ; EDTA ; Escherichia coli ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Extraction of intracellular protein from Escherichia coli is traditionally achieved by mechanical disruption. A chemical treatment that destroys the integrity of the bacterial cell wall and could provide an alternative technique is examined in this study. Treatment with a combination of the chelating agent ethylenediaminetet-raacetate (EDTA) (greater than 0.3 mM) and the chaotropic agent urea (6 M) is highly effective at releasing protein from uninduced E. coli. The 6 M urea in the presence of 3 mM EDTA can release cytoplasmic protein from both logarithmic-phase and stationary-phase E. coli cells at levels equivalent to mechanical disruption. The concentrations of the two chemical agents were the major variables affecting the maximum levels of protein release. Several minor variables and interactions were also identified. The kinetics of protein release is first order. For 2, 4, and 6 M urea with 3 mM EDTA, the time constant is approximately 2.5 min independent of urea concentration. Kinetics for 3 mM EDTA without urea is considerably slower, with a time constant of 12.3 min. © 1997 John Wiley & Sons, Inc. Biotechnol Bioeng 53: 453-458, 1997.
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  • 52
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    Biotechnology and Bioengineering 53 (1997), S. 487-496 
    ISSN: 0006-3592
    Keywords: bacterial chemotaxis ; Escherichia coli ; random motility ; mathematical model ; sand core ; porous media ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: The migration of chemotactic bacteria in liquid media has previously been characterized in terms of two fundamental transport coefficients - the random motility coefficient and the chemotactic sensitivity coefficient. For modeling migration in porous media, we have shown that these coefficients which appear in macroscopic balance equations can be replaced by effective values that reflect the impact of the porous media on the swimming behavior of individual bacteria. Explicit relationships between values of the coefficients in porous and liquid media were derived. This type of quantitative analysis of bacterial migration is necessary for predicting bacterial population distributions in subsurface environments for applications such as in situ bioremediation in which bacteria respond chemotactically to the pollutants that they degrade.We analyzed bacterial penetration times through sand columns from two different experimental studies reported in the literature within the context of our mathematical model to evaluate the effective transport coefficients. Our results indicated that the presence of the porous medium reduced the random motility of the bacterial population by a factor comparable to the theoretical prediction. We were unable to determine the effect of the porous medium on the chemotactic sensitivity coefficient because no chemotactic response was observed in the experimental studies. However, the mathematical model was instrumental in developing a plausible explanation for why no chemotactic response was observed. The chemical gradients may have been too shallow over most of the sand core to elicit a measurable response. © 1997 John Wiley & Sons, Inc. Biotechnol Bioeng 53: 487-496, 1997.
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  • 53
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    Keywords: recombinant protein production ; Escherichia coli ; heparinase ; bioprocess simulation ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Heparinase I from flavobacterium heparinum has several potential clinical applications; the resulting high demands on protein purity and quantity can be met by recombinant expression in Escherichia coli. Based on laboratory scale experiments with insoluble heparinase I expression followed by renaturation, a process for production of 3 kg/year of heparinase I was designed. We present a comparative analysis of the production costs of soluble and insoluble heparinase I expression, as well as a generalized approach to sensitivity analysis, based on perturbation around a base case design scenario. This may assist focusing further development on process steps for which improvements both are feasible and result in significant cost saving. © 1997 John Wiley & Sons, Inc. Biotechnol Bioeng 53: 575-582, 1997.
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  • 54
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    Biotechnology and Bioengineering 50 (1996), S. 108-114 
    ISSN: 0006-3592
    Keywords: β-galactosidase ; overexpression ; runaway replication vectors ; translational fusions ; Escherichia coli ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: To determine the utility of coupling runaway replication to the expression of cloned genes under the control of strong promoters, lacZ transcriptional fusions to the trp or tac promoter (Ptrp or Ptac) were constructed using plasmids in which the copy number is thermally regulated. Cells containing these plasmids were able to produce β-galactosidase to levels between 3700 and 46,000 Miller units when induced only by a temperature upshift. The addition of the appropriate chemical inducer, either IPTG (isopropyl-β-D-thiogalactopyranoside) or IAA (3-β-indoleacrylic acid), did not significantly enhance the thermal induction. The Ptac-controlled and Ptrp-controlled lacZ induction differed slightly in that the Ptac-controlled thermal induction exhibited a lag of approximately 1.5 h as compared to both chemical and thermal induction, whereas in the case of Ptrp-controlled induction, an increase in β-galactosidase expression above background occurred at approximately the same time regardless of the means of induction. The best vector, a Ptrp-controlled lacZ fusion carried on a runaway replication vector having a basal copy number of 10, was able to mediate the expression of β-galactosidase to approximately 40,000 Miller units of β-galactosidase comprising 25% of the total cell protein at 17 h postinduction under optimal conditions for protein yield. In these cells, lysis occurred as lacZ was maximally expressed. Under noninducing conditions, the plasmids were stable for at least 60 generations in the absence of antibiotic in batch culture. © 1996 John Wiley & Sons, Inc.
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  • 55
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    Biotechnology and Bioengineering 51 (1996), S. 434-438 
    ISSN: 0006-3592
    Keywords: polyphosphate ; Escherichia coli ; phosphate starvation ; gene expression ; heterologous ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: The effect of intracellular polyphosphate on the phosphate-starvation response in Escherichia coli was studied by genetically manipulating the intracellular polyphosphate levels and by performing phosphate shifts on the genetically engineered strains. Strains that produced large quantities of polyphosphate and were able to degrade it induced the phosphate-starvation response to a lesser extent than wild-type strains, whereas strains that were unable to degrade a large intracellular polyphosphate pool induced the phosphate-starvation response to a greater extent than wild-type strains. These results have important implications for expression of heterologous genes under control of the phoA promoter. © 1996 John Wiley & Sons, Inc.
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  • 56
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    Biotechnology and Bioengineering 60 (1998), S. 230-238 
    ISSN: 0006-3592
    Keywords: Escherichia coli ; metabolism ; flux ; linear optimization ; biomass composition ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: The amino acid composition of proteins and the fatty acid composition of the cell membranes were measured in Escherichia coli growing exponentially in batch culture on glucose, succinate, glycerol, pyruvate, and acetate, and growing under continuous culture conditions on glucose at dilutions rates equivalent to the growth rates of the batch cultures. Although the fatty acid composition of the membranes did change significantly with carbon source and dilution rate, the amino acid content of proteins did not change significantly under either condition. A previously developed stoichiometric model of metabolism was used to calculate the fluxes through the metabolic reactions and to determine their sensitivity to changes in fatty acid and amino acid composition. © 1998 John Wiley & Sons, Inc. Biotechnol Bioeng 60: 230-238, 1998.
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  • 57
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    Biotechnology and Bioengineering 38 (1991), S. 340-352 
    ISSN: 0006-3592
    Keywords: Immobilized cells ; Escherichia coli ; microfluorimetry ; DNA staining ; DNA synthesis ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Pronounced spatial nonuniformities in cell density, physiology, and activity frequently arise within densely packed immobilized cell supports. For a more fundamental understanding of immobilized cell phenomena, we have developed high-resolution microfluorimetric procedures to analyze local variations in both immobilized cell loading and growth rate. Fluorescent staining of total cellular DNA provides a measure of local biomass density. Actively growing (DNA synthesizing) cells are marked by pulse-labeling newly synthesized DNA with the thymine analog, bromouracil. An immunofluorescent technique allows subsequent detection of spatial variations in DNA synthesis rates. These procedures enable the influence of mass-transfer limitations and other immobilization effects on cell distribution and activity to be readily quantified. We demonstrate this approach through analysis of the patterns of growth of Escherichia coli entrapped within Sr-alginate gel beads. The experimental techniques are potentially applicable to a variety of other aggregate cell systems.
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  • 58
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    Keywords: homogenization, high-pressure ; cell disruption ; inclusion bodies ; size distribution ; centrifuge, analytical ; Escherichia coli ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: The high-pressure homogenization of Escherichia coli, strain JM101, containing inclusion bodies of recombinant porcine somatotropin was investigated. A novel technique employing an analytical disc centrifuge was used to monitor the disruption. This a direct technique which measures cell disintegration rather than soluble protein release. The technique is particularly suited to measurements where the disruption approaches 100%. The disk centrifuge provides a size distribution of the homogenate, and furnishes evidence for the preferential disruption of larger cells. For E. coli containing inclusion bodies, and increase in the cell feed concentration from 145 g/L (wet weight) to 330 g/L resulted is poorer homogenization. Poorer disruption was also obtained by lowering the feed temperature from 20°C to 5°C. Only slight variations in performance were obtained by increasing the feed pH from 7.5 to 9.0 or by storing the feed at 4°C for 24 h prior to disruption. Comparison with uninduced E. coli strain JM101, showed that the disruption obtained is higher for bacteria containing a recombinant inclusion body.
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  • 59
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    Biotechnology and Bioengineering 38 (1991), S. 397-412 
    ISSN: 0006-3592
    Keywords: Escherichia coli ; protein synthesis ; metabolic limitations ; cloned-gene expression ; β-galactosidase ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Earlier experiments in our lab investigated the metabolic limitations of cloned-gene expression in bacterial cells (for over-production of β-lactamase). These experiments showed that the steady-state concentration of ribosomal RNA decreased upon plasmid amplification while both the synthesis rate and steady-state β-lactamase mRNA level increased significantly. This appeared to indicate substantial limitation exist within the transnational machinery of the bacterial cell at high copy numbers. To establish the generality of this phenomenon, the impact increasing protein expression from pa plasmid by chemically inducing a strong promoter while maintaining constant copy number has been investigated. A plasmid has been constructed which contains the lacZ gene under control of the tac promoter and contains the parB stability locus to maintain plasmid stability. Using this vector, β-galactosidase expression in chemostat cultures operated at specific growth rates of 0.6 h-1 was induced with IPTG such that enzyme activity was varied over a 460-fold range. When fully induced β-galactosidase protein production represented 14 wt % of total cell protein. As transcription was induced, the synthesis rate of the β-galactosidase mRNA increased 42-fold while the steady-state level of β-galactosidase mRNA increased only fourfold. This indicates stability may play a larger role for β-galactosidase expression with a strong promoter than seen with β-lactamase production in the elevated copy number system. Furthermore, rRNA synthesis rates increased at high expression rates as seen in the copy number experiments. However, unlike the amplified-plasmid system, the steady-state levels of rRNA increased as well. Since the total protein levels closely followed the steady-state level of eRNA, transnational limitations are again suggested for the chemically induced transcription system.
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    Biotechnology and Bioengineering 39 (1992), S. 663-671 
    ISSN: 0006-3592
    Keywords: Escherichia coli ; acetic acid ; methionine ; yeast extract ; continuous fermentation ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Acetic acid formation in Escherichia coli fermentation has been studied in continuous cultures. Experimental results suggest that the limited capacity of the oxidative metabolism (perhaps the limited capacity of TCA cycle) may be responsible for acetic acid formation. At low growth rates, both anabolic and catabolic requirements may be satisfied by the oxidative metabolism. However, at high growth rates these two demands may exceed the capacity of the oxidative metabolism alone. It is proposed that under these circumstances, E. coli reorganizes the oxidative metabolism to first meet the anabolic requisition and then supply the necessary amount of energy using both the remaining capacity of the oxidative metabolism and acetic acid formation metabolism. Escherichia coli selects acetic acid synthesis as the aerobic energy source because it generates the second largest amount of ATP and NADH2. According to our proposition, acetic acid formation could be reduced by decreasing the anabolic requirement, i.e., reducing glucose uptake, or by increasing the capacity of the oxidative metabolism. These two approaches were experimentally confirmed by observing reduced acetic acid formation by reducing the glucose uptake with a yeast extract addition and enhancing the capacity of oxidative metabolism with a methionine addition.
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    Biotechnology and Bioengineering 39 (1992), S. 775-780 
    ISSN: 0006-3592
    Keywords: formate ; Escherichia coli ; formate hydrogenlyase ; cell immobilization ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Formate hydrogenlyase (FHL) activity was induced in a strain of Escherichia coli S13 during anaerobic growth in yeast extract-tryptone medium containing 100 mM formate. The cells obtained at the optimum growth phase were immobilized in 2.5% (w/v) agar gel when 50-60% of the whole cell FHL activity was retained. The immobilized FHL system had good storage stability and recycling efficiency. In the lysis of formate, an increase of formate concentration to 1.18M increased QH2 (initial) value of the immobilized cell, and subsequently cells, hydrogen evolution, in general, ceased after 6 to 8 of incubation, resulting in incomplete lysis of formate. Presence of small amount of glucose (28 mM) was more or less quantitatively lysed with concomitant disappearence of glucose from the medium. Synthesis of formate from hydrogen and bicarbonate solution by the immobilized cells was also characterized. Presence of glucose (10 mM) in 50 mM bicarbonate solution stimulated formate synthesis by immobilized cells. The pH optimum range, Km, and specific activity of the immobilized cells for the lysis of formate were 6.8-7.2 0.4M, and 66 mL/g cell-h, respectively. The cells could fix hydrogen to the extent of 24.4% (w/w) of its own wet cell mass in a 72-h reaction cycle. Potentiality of the immobilized FHL system for biotechnological exploitation was discussed.
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    Biotechnology and Bioengineering 41 (1993), S. 3-13 
    ISSN: 0006-3592
    Keywords: recombinant protein ; Escherichia coli ; inclusion body ; renaturation ; disulfide bond ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Expression of recombinant proteins in Escherichia coli often results in the formation of insoluble inclusion bodies, In case of expression of eukaryotic proteins containing cysteine, which may form disulfide bonds in the native active protein, often nonnative inter- and intramolecular disulfide bonds exist in the inclusion bodies. Hence, several methods have been developed to isolate recombinant eukaryotic polypeptides from inclusion bodies, and to generate native disulfide bonds, to get active proteins. This article summarizes the different steps and methods of isolation and renaturation of eukaryotic proteins containing disulfide bonds, which have been expressed in E. coli as inclusion bodies, and shows which methods originally developed for studying the folding mechanism of naturally occurring proteins have been successfully adapted for reactivation of recombinant eukaryotic proteins. © 1993 John Wiley & Sons, Inc.
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  • 63
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    Biotechnology and Bioengineering 41 (1993), S. 937-946 
    ISSN: 0006-3592
    Keywords: protein excretion ; continuous culture ; Escherichia coli ; β-lactamase ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: The stable continuous overproduction of a plasmidencoded protein, β-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 β-lactamase could not be sustained with this strain in a single-stage chemostat because of cell death and selection for lac-1 cells. β-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 β-lactamase levels. The best operating conditions found at 20°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 β-lactamase was produced at a level of 25% of total cellular protein with 90% excretion yielding 300 mg β-lactamase/L that was 50% pure at an OD600 〈 6. © 1993 Wiley & Sons, Inc.
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  • 64
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    Biotechnology and Bioengineering 42 (1993), S. 215-221 
    ISSN: 0006-3592
    Keywords: on-line NMR ; phosphorus-31 NMR ; Escherichia coli ; aerobic and anaerobic metabolism ; intracellular pH ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: An experimental system has been constructed which enables on-line measurements of phosphorus-31 (31P) nuclear magnetic resonance (NMR) spectra for growing bacterial suspensions under anaerobic or aerobic conditions. A sample stream from a laboratory bioreactor is circulated to the NMR sample chamber in a gas exchange system which permits maintenance of aerobic conditions for high-cell-density cultures. 31P NMR spectra with resolution comparable with those obtained traditionally using dense, concentrated, nongrowing cell suspensions can be obtained at cell densities above 25 g/L with acquisition times ranging from 14 to 3 minutes which decline as cell density increases. This system has been employed to characterize the changes in intracellular state of a stationary phase culture which is subjected to a transition from aerobic to anaerobic conditions. Both intracellular NTP level and cytoplasmic pH are substantially lower under anaerobic conditions. Also, the system has been employed to observe the response of a growing culture to external addition of acetate. Cells are able to maintain pH difference across the cytoplasmic membrane at extracellular acetate concentrations of 5 and 10 g/L. However, acetate concentrations of 20 g/L cause collapse of the transmembrane ΔpH and sharp reduction of the growth rate of the culture. The experimental configuration described should also permit NMR observations of many other types of microbial cultures and of other nuclei. © 1993 John Wiley & Sons, Inc.
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    Biotechnology and Bioengineering 42 (1993), S. 1190-1198 
    ISSN: 0006-3592
    Keywords: fermentation ; bioprocess monitoring ; bioluminescence ; inner filter effect ; Escherichia coli ; cell concentration monitoring ; fiber optic ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Bioluminescence has recently become a popular research tool in several fields, including medicine, pharmacology, biochemistry, bioprocessing, and environmental engineering. Beginning with purely qualitative goals, scientists are now targeting more demanding applications where accurate, quantitative interpretation of bioluminescence is necessary. Using the recent advances in fiber-optic technology, bioluminescence is easily monitored in vivo and in real time. However, the convenience of this measurement is often concealing an unsuspected problem: the bioluminescence signal might be corrupted by a large error caused by the extinction of light by biological cells. Since bioluminescent cultures not only emit light but also absorb and scatter it, the measured signal is related in a complex, nonlinear, and cell-concentration-dependent manner to the “true” bioluminescence. This light extinction effect, known as the “inner filter effect,” is significant in high-density cultures. Adequate interpretation of the bioluminescence signal can be difficult without its correction. Here, we propose a real-time algorithm for elimination of the inner filter effect in a bioreactor. The algorithm yields the bioluminescence which would be measured if the glowing culture was completely transparent. This technique has been successfully applied to batch and continuous cultivation of recombinant bioluminescent Escherichia coli. © 1993 John Wiley & Sons, Inc.
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    Biotechnology and Bioengineering 41 (1993), S. 1092-1100 
    ISSN: 0006-3592
    Keywords: high cell density cultivation ; Escherichia coli ; XAD adsorbents ; dialysis reactor ; controlled substrate feed ; inhibitory products, removal of ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: 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. © 1993 Wiley & Sons, Inc.
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    Biotechnology and Bioengineering 44 (1994), S. 329-336 
    ISSN: 0006-3592
    Keywords: biofilm formation ; Escherichia coli ; C/N ratio ; plasmid retention ; extracellular polysaccharide ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Biofilm formation and plasmid segregational instability in biofilm cultures of Escherichia coli DH5α (pMJR1750) were investigated under different medium-carbon-to-nitrogen (C/N) ratios. At C/N ratios of 0.07 and 1, net accumulation of both biofilm plasmid-bearing and plasmid-free cells continued through the entire experiment without attaining any apparent steady state. At C/N ratios of 5 and 10, net biofilm cell accumulation for the two populations reached apparent steady states after 84 and 72 h, respectively. At C/N ratios of 0.07 and 1, polysaccharide production increased slowly and reached about 2g alginate equivalent/cm2 by the end of both experiments. At a C/N ratio of 5, polysaccharide increase significantly after 84 h, reaching about 7μg alginate equivalent/cm2 prior to termination. At a C/N ratio of 10, polysaccharide increased significantly after 72 h and reached 21 μg alginate equivalent/cm2 at 108 h. At C/N ratios of 0.07 and 1, protein production reached 6.5 and 4 μg/cm2, respectively. At C/N ratios of 5 and 10, protein production increased slightly for the first 84 h and reached a maximum at 108 h, at 3 and 2 μg/cm2, respectively, then decreased over the last 12 h of the experiment. Ratios of polysaccharide to protein increased with increasing C/N ratios. At C/N ratios of 0.07 and 1, the ratios between extracellular polysaccharide (EP) and protein were no more than 205 μg polysaccharide/μg protein, whereas those at C/N ratios of 5 and 10 increased to about 7 and 12 μg polysaccharide/μg protein, respectively.Probabilities of plasmid loss in the biofilm cultures increased with increasing C/N ratios. At C/N ratios of 0.07, 1, and 5, the probabilities of plasmid loss were 0.0013 ± 0.011, 0.020 ± 0.006 and 0.122 ± 0.021, respectively. At a C/N ratio of 10, the probability of plasmid loss was significantly higher, reaching 0.38 ± 0.125. The increase of probability of plasmid loss at higher C/N ratios results from competition between cell replication and extracellular polysaccharide production. © 1994 John Wiley & Sons, Inc.
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    Biotechnology and Bioengineering 48 (1995), S. 149-157 
    ISSN: 0006-3592
    Keywords: mass transfer ; Escherichia coli ; cell cultures ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Nutrient depletion and inhibitory end-product accumulation are the major problems for hydrogel-entrapment cell cultures. An electrokinetic technique was developed to enhance intrahydrogel mass transfer to overcome these problems. Escherichia coli cells (ATCC 15224) were entrapped in 3.2-mm-thick potassium-K-carrageenan and agarose hydrogel slabs. With a electric current density of 180A/m2 the cell densities were increased by 140%(from 3.9 to 9.6 dry cell weight [DCW] g/L) in potassium-K-carrageenan and by 80% (from 3.9 to 7.0 DCW g/L) in agarose. A mathematical model taking into account nutrient depletion, inhibitory end-product formation, and cell growth kinetics under facultatively anaerobic conditions was developed to rationalize the overall transport and biological behaviors in the hydrogel. The cell growth in hydrogel was successfully simulated. It is concluded that the augmented transports for glucose and inhibitory end-products accounted for these increases in cell growth. The increase in cell density in potassium-K-carrageenan was due to the enhanced removal of inhibitory end-products (through electroosmosis and electro-phoresis: 80%) and due to the augmented glucose transport (through electroosmosis: 20%). © 1995 John Wiley & Sons, Inc.
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    Biotechnology and Bioengineering 38 (1991), S. 314-318 
    ISSN: 0006-3592
    Keywords: Escherichia coli ; maltoporin ; harvesting bacteria ; bacterial surfaces ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Addition of starch to suspensions of Escherichia coli K-12 resulted in the formation of bacterial flocs. The flocculation was dependent on the high expression of a receptor for starch (maltoporin) on the surface of the bacterium. Factors influencing floc formation were investigated and optimal conditions for flocculation based on cell density, starch concentration, time, and pH established. As quantitated by a sedimentation assay, over 80% of bacteria in a culture could be removed by settling without centrifugation in 3 h under optimal conditions. Floc formation was evident with bacteria containing wild-type maltoporin but was faster and occurred to a greater extent with strains expressing a high-affinity allele (lamB1400) of the starch receptor. Bacteria could be harvested by floc formation directly in growth medium under defined conditions of maltoporin expression and medium composition. These results demonstrate the effectiveness of starch-dependent aggregation in the harvesting of cells, using an inexpensive, biologically acceptable agent to induce flocculation.
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    Biotechnology and Bioengineering 37 (1991), S. 661-672 
    ISSN: 0006-3592
    Keywords: bacterial chemotaxis ; Escherichia coli ; random motility ; diffusion chamber assay ; mathematical model ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: A quantitative description of bacterial chemotaxis is necessary for making predictions about the migratory behavior of bacterial populations in applications such as biofilm development, release of genetically engineered bacteria into the environment, and in situ bioremediation technologies. The bacterial chemotactic response is characterized by a mathematical model which relates individual cell properties such as swimming speed and tumbling frequency to population parameters, specifically the random motility coefficient and the chemotactic sensitivity coefficient. Our model includes a nonlinear dependence of the chemotactic velocity on the attractant gradient as well as a dependence of the random motility coefficient on the temporal and spatial attractant gradients, both of which previous analyses have neglected. As we will show, these aspects are critical for interpreting the results from experiments like those performed in the stopped-flow diffusion chamber (SFDC) because the initial temporal and spatial gradients are very steep. Our analysis demonstrates that values for the random motility coefficient and chemotactic sensitivity coefficient can be obtained from experimental plots of net cell redistribution from initial conditions versus the square root of time. Values for these parameters are determined from experimental measurements of bacterial population distributions in the SFDC as described in the companion article. Using parameter values determined from independent experiments, μ = 1.1 ± 0.4 ± 10-5 cm2/s and χ0 = 8 ± 3 ± 10-5 cm2/s, excellent agreement is found between theoretically predicted bacterial density profiles and actual experimental profiles for Escherichia coli K12 responding to fucose over two orders of magnitude in initial attractant concentration. Thus, our model captures the concentration dependence of this behavioral response satisfactorily in terms of cell population parameters which are derived from individual cell properties and will therefore be useful for making predictions about the migratory behavior of bacterial populations in the environment.
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  • 71
    ISSN: 0006-3592
    Keywords: Escherichia coli ; growth factor ; epidermal growth factor ; fed batch culture ; human epidermal growth factor ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Fed-batch cultures of recombinant E. coli HB101 harboring expression plasmid pTRLBT1 or pTREBT1, with acetate concentration monitoring, are investigated to obtain high cell density and large amounts of human epidermal growth factor (hEGF). The expression plasmid pTRlBT1 contains a synthetic hEGF gene attached downstream of the N-terminal fragment of the trp L gene preceded by the trp promoter. The expression plasmid pTREBT1 contains the same coding sequence attached downstream of the N-terminal fragment of the trp E gene preceded by the trp promoter, trp L gene, and attenuator region. E. coli harboring pTREBT1 produces 0.56 mg/L hEGE and immediately degrades it. On the other hand E. coli harboring pTRLBT1 produces 6.8 mg/L hEGF and does not decompose it. Prominent inclusion bodies are observed in E. coli cells harboring pTRLBT1 using an election microscope. To Cultivate E. coli harboring pTRLBT1, a fed-batch culture system, divided into a cell growth step and an hEGF production step, is carried out. The cells grow smoothly without acetate-induced inhibition. Cell concentration and hEGF quantity reach the high values of 21 g/L and 60 mg/L, respectively.
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  • 72
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    Biotechnology and Bioengineering 38 (1991), S. 831-837 
    ISSN: 0006-3592
    Keywords: fermentation ; Escherichia coli ; recombinant fermentation ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: The effects of dilution rates on the performance of a two-stage fermentation system for a recombinant Escherichia coli culture were studied. Dilution rate determines the apparent or averaged specific growth rate of a heterogeneous population of cells in the recombinant culture. The specific growht rate affects the genetic parameters involved in product formation in the second stage, such as plasmid stability, plasmid content, and specific gene expression rate. Kinetic models and correlations were developed for these parameters based on experimental data. Simulations of plasmid stability in the first stage showed that for longer fermentation periods, plasmid stability is better at higher dilution rates. However, the plasmid content is lower at these dilution rates. The optimal apparent specific growth rate for maximum productivity in the second stage was determined using two methods: (1) direct search for a constant specific growth rate, and (2) dynamic optimization using the maximum principle for a time-dependent specific growth rate profile. The results of the calculations showed that the optimum constant apparent specific growth rate for maximum over-all productivity is 0.40 h-1. This coincides with the optimal specific growht rate for maximum plasmid content in the expressed stage. A 3.5% increase in overall productivity can be obtained by using a linear time dependent apparent specific growth rate control, μ2(t) = 0.0007t, in the course of the fermentation time.
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  • 73
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    Biotechnology and Bioengineering 38 (1991), S. 891-906 
    ISSN: 0006-3592
    Keywords: ribosome vector ; cloned-gene expression ; Escherichia coli ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: An expression system utilizing specialized ribosomes has been constructed with β-galactosidase as the product. Ribosomes specific for lacZ mRNA are generated due to a mutation within the anti-Shine-Dalgarno region of a plasmidborne 16S rRNA gene that is complementary to a mutation within the ribosome-binding site of lacZ. Hence, a subpopulation of ribsomes specific for translation of the cloned gene mRNA is produced. Transcription of the lacZ gene is regulated by the tac promoter, while transcription of the mutated rrnB locus is controlled by the λPL promoter. Batch experiments indicate that full induction of both operons (2 mM IPTG, 42°C) leads to maximal β-galactosidase activity per cell at levels 35% higher than that obtained using a wild-type ribosome expression system. Using a novel, site-directed mutagenesis technique, construction of the specialized ribosome vector is outlined, and the results of lacZ expression are presented as transcription of both the cloned-gene and the specialized-ribosome locus are induced.
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  • 74
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    Biotechnology and Bioengineering 39 (1992), S. 225-232 
    ISSN: 0006-3592
    Keywords: electroconductive heating ; electrical pretreatment ; thermal death kinetics ; zygo Saccharomyces bailii ; Escherichia coli ; microorganisms ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Suspensions of yeast cell (zygo Saccharomyces bailii) in a phosphate buffer solution were subjected to conventional (hot water) and ohmic (electric current) heating under identical temperature histories. Experiments were also conducted with cells of Escherichia coli to compare the lethal effect of combination of sublethal electrical preteatment and conventional heating with conventional heating. The kinetic parameters (D,Z,K and Ea) were determined for both organisms during different treatments. There was no significant difference in the death rate of yeast cells during conventional and ohmic heating at the voltage range used in this study. Results of electrical pretreatment and conventional heating on E. coli indicated differences under certain conditions when compared with pure conventional heating. Thus it is concluded that microbial death during ohmic heating was due primarily to thermal effects with no significant effect of electric current per se. Sublethal electrical pretreatment appears to offer potential for increased bacterial inactivation in certain cases.
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  • 75
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    Biotechnology and Bioengineering 39 (1992), S. 398-407 
    ISSN: 0006-3592
    Keywords: recombinant bacterium ; plasmid stability ; filtering ; smoothing ; Escherichia coli ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: A numerical method to process experimental data concerning plasmid stability of a recombinant bacteria during continuous cultures with nonselective media is proposed here. This method differs from previous ones in that it uses the derivatve form of the state equation of the Imanaka-Aiba model for recombinant cultures. The methodology proposed here allows one to estimate values for the two model parameters without forcing them to be constant. Until now, this could not be done using classical analytical techniques because these parameters have been considered invariable because of the integration used in the evaluation of the model. These parameters are (1) the difference in the specific growth rates between plasmid-carrying cells and plasmid-free cells (δμ), and (2) the probability of plasmid loss by plasmid-containing cells (ρr μ+). The derivative technique used here is completed by mathematical treatments involving data filtering and smoothing. The values of the two parameters are in agreement with those already publised. The current technique does not impose preconditions and permit us to further study related phenomena.
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  • 76
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    Biotechnology and Bioengineering 40 (1992), S. 334-336 
    ISSN: 0006-3592
    Keywords: sampling, automatic containment ; Escherichia coli ; fermentation ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: A containment sampling system for shake flasks and fermentors has been developed from a blood collection system used in hospitals. The core of the system is a collection vial with a vacuum inside. When a needle connected to the fermentation fluid penetrates a rubber seal on the vial, a sample is withdrawn. The system has been developed in two versions, a manual method for shake flasks, and an automated version for fermentors including cool storage of samples. The sampling system offers the same safety for fermentation containment as the original system offers safety for patients and hospital staff. © 1992 John Wiley & Sons, Inc.
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  • 77
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    Biotechnology and Bioengineering 41 (1993), S. 237-244 
    ISSN: 0006-3592
    Keywords: Escherichia coli ; iron transport ; enterobactin HPLC ; dialysis membrane fermentor ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: The article describes four different fermentation procedures for Escherichia coli AN311, a producer of enterobactin. A regular rotary shaker culture with a biphasic system consisting of an agar layer (as a reservoir for feeding processes) and a layer of liquid medium, 2.4 L and 10 L batch cultures, and a novel dialysis membrane fermentor were used. With the use of this latter fermentor type, the production of enterobactin could be increased by a factor of about 9.5, while growth increased by a factor of 12 compared to the other systems. For the rapid and reliable quantification of the concentration and purity of enterobactin an analytical and preparative high-performance liquid chromatography (HPLC) method was established. The degradation compounds of this siderophore were detected by diodearray and bioassays. A comparison of total catechol production as well as the distribution between enterobactin and its degradation compounds is given. © 1993 John Wiley & Sons, Inc.
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  • 78
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    Biotechnology and Bioengineering 41 (1993), S. 325-329 
    ISSN: 0006-3592
    Keywords: chemostat ; enzyme overproduction ; plasmid stability ; Escherichia coli ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: The effect of plasmid-mediated metabolic burden of on the expression of the host genes and its consequences on the plasmid maintenance were studied in carbon-limited chemostat culture of Escherichia coli 1EA(pBR322) subject to selection for strains overproducing chromosomally coded ribitol dehydrogenase. The chemostat population became rapidly heterogeneous and the competition among evolved strains was found to be crucial for the kinetics of the plasmid loss from the culture. The selective disadvantages in growth rate associated with plasmid carriage in the parent-like and ribitol dehydrogenase-overproducing strains was estimated. © 1993 John Wiley & Sons, Inc.
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  • 79
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    Biotechnology and Bioengineering 40 (1992), S. 271-279 
    ISSN: 0006-3592
    Keywords: carbon starvation ; Escherichia coli ; growth control ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: The use of glucose starvation to uncouple the production of recombinant β-galactosidase from cell growth in Escherichia coli was investigated. A lacZ operon fusion to the carbon starvation-inducible cst-1 locus was used to control β-galactosidase synthesis. β-Galactosidase induction was observed only under aerobic starvation conditions, and its expression continued for 6 h following the onset of glucose starvation. The cessation of β-galactosidase expression closely correlated with the exhaustion of acetate, an overflow metabolite of glucose, from the culture medium. Our results suggest the primary role of acetate in cst-1-controlled protein expression is that of an energy source. Using this information, we metered acetate to a glucose-starved culture and produced a metabolically sluggish state, where growth was limited to a low linear rate and production of recombiant β-galactosidase occurred continuously throughout the experiment. The cst-1 controlled β-galactosidase synthesis was also induced at low dilution rates in a glucose-limited chemostat, suggesting possible applications to high-density cell systems such as glucose-limited recycle reactors. This work demonstrates that by using an appropriate promoter system and nutrient limitation, growth can be restrained while recombinant protein production is induced and maintained.
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  • 80
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    Biotechnology and Bioengineering 41 (1993), S. 557-565 
    ISSN: 0006-3592
    Keywords: amino acid addition ; protein stability ; stress response ; Escherichia coli ; chloramphenicol-acetyl-transferase ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: In this work, effective feeding schemes that would minimize stress responses to cloned-protein overexpression are investigated. The cloned-protein (chloramphenicolacetyl-transferase, CAT) contains a high aromatic amino acid content, most notably a high phenylalanine content. Experiments performed on Escherichia coli RR1 [pBR329] (constitutive promoter) and E. coli JM105 [pSH101] (inducible promoter) demonstrated that phenylalanine addition increases the rate of synthesis and yield of CAT. A previous study correlating inducer strength with CAT expression in E. coli JM105 [pSH101] indicated that the highest expression rate was accompanied by the highest apparent rate of protein degradation. In this work, the combined addition of isopropyl-β-D-thiogalactopyranoside (IPTG) and phenylalanine at intermediate levels resulted in substantial increase of CAT synthesis and partial reduction of protein degradation. Furthermore, transmission electron micrographs verified the absence of inclusion bodies, which, along with proteases, were suspected to reduce protein activity. The research demonstrates that significant enhancement in production and stability of heterologous proteins is possible by designing feeding strategies that incorporate knowledge of the interaction between primary cellular metabolism and foreign protein expression. © 1993 John Wiley & Sons, Inc.
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  • 81
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    Biotechnology and Bioengineering 43 (1994), S. 847-855 
    ISSN: 0006-3592
    Keywords: Escherichia coli ; cellular energetics ; acetate production ; carbon yield ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: An integrated metabolic model for the production of acetate by Escherichia coli growing on glucose under aerobic conditions was presented previously (Ko et al., 1993). The resulting model equations can be used to explain phenomena often observed with industrial fermentations, i.e., increased acetate production which follows from high glucose uptake rate, a low dissolved oxygen concentration, a high specific growth rate, or a combination of these conditions. However, several questions still need to be addressed. First, cell composition is growth rate and media dependent. Second, the macromolecular composition varied between E. coli strains. And finally, a model that represents the carbon fluxes between the Embden-Meyerhof-Parnas (EMP) and the hexose monophosphate (HMP) pathways when cells are subject to internal and/or external stresses is still not well defined. In the present work, we have made an effort to account for these effects, and the resulting model equations show good agreement for wild-type and recombinant E. coli experimental data for the acetate concentration, the onset of acetate secretion, and cell yield based on glucose. These results are useful for optimizing aerobic E. coli fermentation processes. More specifically, we have determined the EMP pathway carbon flux profiles required by the integrated metabolic model for an accurate fit of the acetic acid profile data from a wild-type E. coli strain ML308. These EMP carbon flux profiles were correlated with a dimensionless measurement of biomass and then used to predict the acetic acid profiles for E. coli strain F-122 expressing human immunodeficiency virus-(HIV528) β-galactosidase fusion protein. The effect of different macromolecular compositions and growth rates between these two E. coli strains required a constant scaling factor for improved quantitative predictions.
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  • 82
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    Biotechnology and Bioengineering 44 (1994), S. 539-548 
    ISSN: 0006-3592
    Keywords: cross-flow filtration ; Escherichia coli ; cell harvesting ; fermentation ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Cross-flow filtration of Escherichia coli strains was examined at the laboratory and pilot scales using Romicon 500,000 molecular-weight-cutoff hollow fiber membranes. Both the series resistance and macrosolute polarization models were employed to compare performances. Total dissolved solids content above 90 g/L and viscosity above 1.1 × 10-3 paċ s of cell-free culture media were found to decrease average filtration fluxes by over 60% both in the absence and presence of cells. Broth filtration with culture media of dissolved solids levels below 80 g/L were influenced to a greater extent by harvest cell density. The collodial nature of the complex nutrient responsible for the total solids increase affected prediction of filtration performance. Differences in strain filterability were observed with JM109 preferred over DH5 in high solids-containing media and RR1 preferred over JM109 in low dissolved solids-containing media. Their research demonstrates the importance of cell strain and media selection in the performance of early downstream processing steps. © 1994 John Wiley & Sons, Inc.
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  • 83
    ISSN: 0006-3592
    Keywords: acetate reduction ; Bacillus subtilis ; Escherichia coli ; cloning ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: A novel metabolic engineering technique involving the redirection ofcellular carbon fluxes was employed to reduce acetate production in an Escherichia coli culture. Metabolic engineering was achieved by cloning E. coli the gene for the Bacillus subtilis acetolactate synthase (ALS), an enzyme capable of catalyzing the conversion of pyruvate to nonacidic and less harmful species. The heterologous expression of the ALS catabolic enzyme in Escherichia coli drastically modified the cellular glycolytic fluxes. In particular, acetate excretion, which is a common characteristic of E. coli, as well as a physiological burden, was minimized. The residual acetate level was kept under control and maintained at a level that was below the toxic threshold. The expression of the biologically active ALS enzyme in E. coli did not result in any detectable changes on either cell growth rate or cell yields. The alternative product, acetoin, was shown to be 50 times less harmful than acetate. Similarities in the growth pattern of two different E. coli strains, RR1 and GJT001, under all cultivation conditions suggested that the ability of ALS to reduce acetate accumulation is generic and not strain-specific. © 1994 John Wiley & Sons, Inc.
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    Biotechnology and Bioengineering 44 (1994), S. 952-960 
    ISSN: 0006-3592
    Keywords: Escherichia coli ; protein production, recombinant ; glucose uptake ; acetate excretion ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Reduction of acetate excretion using a modified cellular glucose uptake rate was examined. An Escherichia coli strain bearing a mutationin ptsG, a gene encoding enzyme II in glucose phosphotransferase system (PTS), was constructed and characterized. The growth rate of the mutant strain was slower than its parent in glucose defined medium, butwas not affected in complex medium. Experimental results using this mutant strain showed a significant improvement in culture performance in simple batch cultivations due to reduced acetate excretion through the modified glucose uptake. Both biomass and recombinant protein productivity were increased by more than 50% with the ptsG mutant when compared to the parent strain. Recombinant protein productivity by the newly constructed strain at a level of more than 1.6 g/L was attained consistently in a simple batch bioreactor. © 1994 John Wiley & Sons, Inc.
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  • 85
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    Biotechnology and Bioengineering 48 (1995), S. 303-315 
    ISSN: 0006-3592
    Keywords: Plasmid recovery ; Escherichia coli ; Cell disruption ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Five different mechanical cell disruption processes were evaluated as methods to extract plasmids from bacterial cells. The methods used were sonication, nebulization homogenization, microfluidization, and bead milling. The recovery yields of intact plasmids from the various methods were measured by quantitative gel electrophoresis. Bead milling and microfluidization were found to have the highest potential for large scale extraction with total intact recoveries of over 90% and around 50%, respectively. Other methods resulted in substantial plasmid degradation, with recoveries no greater than 20% of the total intact plasmid. © 1995 John Wiley & Sons, Inc.
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  • 86
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    Biotechnology and Bioengineering 41 (1993), S. 211-220 
    ISSN: 0006-3592
    Keywords: plasmid retention ; gene expression ; biofilm ; β-galactosidase ; segregational instability ; Escherichia coli ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Differences in plasmid retention and expression are studied in both suspended and biofilm cultures of Escherichia coli DH5α(PMJR1750). An alternative mathematical model is proposed which allows the determination of plasmid loss probability in both suspended batch and continuously fed biofilm cultures. In our experiments, the average probability of plasmid loss of E. coli DH5α(pMJR1750) is 0.0022 in batch culture in the absence of antibiotic selection pressure and inducer. Under the induction of 0.17 MM IPTG, the maximum growth rate of plasmid-bearing cells in suspended batch culture dropped from 0.45 h-1 to 0.35 h-1 and the β-galactosidase concentration reached an experimental maximum of 0.32. pg/cell 4 hours after the initiation of induction. At both 0.34 and 0.51 mM IPTG, growth rates in batch cultures decreased to 0.16 h-1, about 36% of that without IPTG, and the β-galactosidase concentration reached an experimental maximum of 0.47 pg/cell 3 hours after induction.In biofilm cultures, both plasmid-bearing and plasmid-free cells in increase with time reaching a plateau after 96 hours n the absence of both the inducer and any antibiotic selection pressure. Average probability of plasmid loss for biofilm-bound E. coli DH5β(pMJR1750) population was 0.017 without antibiotic selection. Once the inducer IPTG was added, the concentration of plasmid-bearing cells in biofilm dropped dramatically while plasmid-free cell numbers maintained unaffected. The β-galactosidase concentration reached a maximum in all biofilm experiments 24 hours after induction; they were 0.08, 0.1, and 0.12 pg/cel under 0.17, 0.34, and 0.51 mM IPTG, respectively. © 1993 John Wiley & Sons, Inc.
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    Biotechnology and Bioengineering 41 (1993), S. 316-324 
    ISSN: 0006-3592
    Keywords: Escherichia coli ; acetic acid ; inhibition ; glycine ; methionine ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Among amino acids screened for their potential to relieve wild and recombinant Escherichia coli from the negative effects of acetic acid, glycine, and methionine showed a sparing effect. In the presence of 2 g/L of acetic acid, addition of 0.5 g/L of glycine or methionine resulted in either a complete recovery or a further enhancement in the specific growth rate, while the enhancement was significant but not fully complete in the presence of 4 g/L of acetic acid. The addition of 0.5 g/L of methionine alleviated the negative effect of acetic acid on recombinant E. Coli growth to produce more β-lactamase, which was encoded by plasmid pUC18. In continuous fermentation the methionine effect on recombinant. E. coli metabolism depended on dilution rate; at high dilution rates, above 0.4 h-1, the methionine addition enhanced β-lactamase production and reduced acetic acid formation, while at low dilution rates, below 0.3 h -1, the effect was reversed. In def-batch fermentation with wild-type E. Coli, cell growth rate and cell yield from glucose were enhanced with methionine addition, while the acetic acid concentration reached over 4 g/L. © 1993 John Wiley & Sons, Inc.
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    Biotechnology and Bioengineering 43 (1994), S. 429-433 
    ISSN: 0006-3592
    Keywords: disinfection ; Escherichia coli ; water disinfection ; activated carbon fiber ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: A novel electrochemical reactor employing activated carbon fiber (ACF) electrodes was constructed for disinfecting bacteria in drinking water. Escherichia coli adsorbed preferentially onto ACF rather than to carbon-cloth or granular-activated carbon. E. coli cells, which adsorbed onto the ACF, were killed electrochemically when a potential of 0.8 V vs. a saturated calomel electrode (SCE) was applied. Drinking water was passed through the reactor in stop-flow mode: 2mL/min for 12 h, o L/min for 24 h, and 1 mL/min for 6 h. At an applied potential of 0.8 V vs, SCE, viable cell concentration reamined below 30 cells/mL. In the absence of an applied potential, bacteria grew to a maximum concentration of 9.5 × 103 cells/mL. After continuous operation at 0.8 V vs. SCE, cells adsorbed onto the ACF could not be observed by scanning electron microscopy. In addition, chlorine in drinking water was completely removed by the reactor. Therefore, clean and efficient inactivation of bacteria in drinking water was successfully performed. © 1994 John Wiley & Sons, Inc.
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    Biotechnology and Bioengineering 43 (1994), S. 399-410 
    ISSN: 0006-3592
    Keywords: lac-based promoters ; Escherichia coli ; genetic control ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: A model that describes induction of protein synthesis from lac-based promoters has been developed and incorporated into the single-cell model of Escherichia coli with transcriptional and translational modifications. Unlike previous models of lac-based promoters, this model allows a priori prediction of the intracellular parameters controlling transcription from lac-based promoters with only the extracellular levels of substrate and inducer as inputs. Because of the structural detail of the model, it is possible to simulate different genetic constructions for comparison, such as Laclq strains versus wild-type cells, or including lacl on a multicopy plasmid. Expression from lac to tac promoters is predicted to yield 5% and 30% of the total cellular protein, respectively, with a pBR322-type plasmid. The model predicts the experimental observation that the Laclq strain is not as fully induced as the wild-type strains, even at higher inducer concentrations. Additionally, the model predicts the right order of magnitude of protein production from lac and tac promoters when mechanisms for attenuation of transcription at lower translational efficiency are considered. Finally, the model predicts that for high copy number systems ribosomes become limiting in the synthesis of plasmid-encoded proteins. © 1994 John Wiley & Sons, Inc.
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    Biotechnology and Bioengineering 43 (1994), S. 969-977 
    ISSN: 0006-3592
    Keywords: cross-flow membrane filtration ; inclusion bodies ; Escherichia coli ; extraction, rIL-2 ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: A cross-flow membrane filtration process was developed for the recovery of rIL-2 inclusion bodies from homogenized Escherichia coli. The membrane extraction process was comprised of a two-step diafiltration followed by an extraction with 7 M GuHCl and a 40-fold dilution of the solubilized inclusion bodies into 0.01 M Tris-HCl, 0.035 M NaCl, pH 7.9. The first diafiltration was with a 0.03 M Tris-HCl, 5 mM ethylenediaminetetraacetic acid (EDTA), pH 8, followed by a diafiltration with 1.75 M GuHCl. All of the insoluble rIL-2 was retained behind the membrane, whereas a GuHCl wash solubilized approximately 15% of the rIL-2. The membrane process increased the yield of rIL-2 in the diluted extract by threefold as compared to a similar centrifuge process with a significant increase in purity as determined by reverse-phase high-performance liquid chromatography (HPLC). © 1994 John Wiley & Sons, Inc.
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    Biotechnology and Bioengineering 44 (1994), S. 1337-1347 
    ISSN: 0006-3592
    Keywords: poly-(3-hydroxybutyric acid) ; PHB ; Escherichia coli ; morphology ; plasmid ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: A stable high-copy-number plasmid pSYL105 containing the Alcaligenes eutrophus polyhydroxyalkanoic acid (PHA) biosynthesis genes was constructed. This plasmid was transferred to seven Escherichia coli strains (K12, B, W, XL1-Blue, JM109, DH5α, and HB101), which were subsequently compared for their ability to synthesize and accumulate ploy- (3-hydroxybutyric acid) (PHB). Growth of recombinant cells and PHB synthesis were investigated in detail in Luria-Bertani (LB) medium containing 20 g/L glucose. Cell growth, the rate of PHB synthesis, the extent of PHB accumulation, the amount of glucose utilized, and the amount of acetate formed varied from one strain to another. XL1-Blue (pSYL105) and B (pSYL105) synthesized PHB at the fastest rate, which was ca. 0.2 g PHB/g true cell mass-h, and produced PHB up to 6-7 g/L. The yields of cell mass, true cell mass, and PHB varied considerably among the strains. The PHB yield of XL1-Blue (pSYL105) in LB plus 20 g/L glucose was as high as 0.369 g PHB/g glucose. Strains W (pSYL105) and K12 (pSYL105) accumulated the least amount of PHB with the lowest PHB yield at the lowest synthesis rate. JM109 (pSYL105) accumulated PHB to the highest extent (85.6%) with relatively low true cell mass (0.77 g/L). Considerable filamentation of cells accumulating PHB was observed for all strains except for K12 and W, which seemed to be due either to the overexpression of the foreign PHA biosynthesis enzymes or to the accumulation of PHB. © 1994 John Wiley & Sons, Inc.
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  • 92
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    Biotechnology and Bioengineering 47 (1995), S. 139-146 
    ISSN: 0006-3592
    Keywords: Escherichia coli ; fed-batch ; acetate ; glucose ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: A Large bioreactor is an inhomogenous system with concentration gradients which depend on the fluid dynamics and the mass transfer of the reactor, the feeding strategy, the saturation constant, and the cell density. The responses of Escherichia coli cells to short-term oscillations of the carbon/energy substrate in glucose limited fed-batch cultivations were studied in a two-compartment reactor system consisting of a stirred tank reactor (STR) and an aerated plug flow reactor (PFR) as a recycle loop. Short-term glucose excess or starvation in the PFR was simulated by feeding of glucose to the PFR or to the STR alternatively. The cellular response to repeated short-term glucose excess was a transient increase of glucose consumption and acetate formation. But, there was no accumulation of acetate in the culture, because it was consumed in the STR part where the glucose concentration was growth limiting. However, acetate accumulated during the cultivation if the oxygen supply in the PFR was insufficient, causing higher acetate formation. The biomass yield was then negatively influenced, which was also the case if the PFR was used to simulate a glucose starvation zone. The results suggest that short-term heterogeneities influence the cellular physiology and growth, and can be of major importance for the process performance. © 1995 John Wiley & Sons, Inc.
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  • 93
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    Biotechnology and Bioengineering 37 (1991), S. 647-660 
    ISSN: 0006-3592
    Keywords: bacterial chemotaxis ; Escherichia coli ; motility, random ; diffusion chamber assay ; mathematical model ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Bacterial chemotaxis, the directed movement of a cell population in response to a chemical gradient, plays a critical role in the distribution and dynamic interaction of bacterial populations in nonmixed systems. Therefore, in order to make reliable predictions about the migratory behavior of bacteria within the environment, a quantitative characterization of the chemotactic response in terms of intrinsic cell properties is needed.The design of the stopped-flow diffusion chamber (SFDC) provides a well-characterized chemical gradient and reliable method for measuring bacterial migration behavior. During flow through the chamber, a step change in chemical concentration is imposed on a uniform suspension of bacteria. Once flow is stopped, diffusion causes a transient chemical gradient to develop, and bacteria respond by forming a band of high cell density which travels toward higher concentrations of the attractant. Changes in bacterial spatial distributions observed through light scattering are recorded on photomicrographs during a 10-min period. Computer-aided image analysis converts absorbance of the photographic negatives to a digital representation of bacterial density profiles. A mathematical model (part II) is used to quantitatively characterize these observations in terms of intrinsic cell parameters: a chemotactic sensitivity coefficient, μ0, from the aggregate cell density accumulated in the band and a random motility coefficient, μ, from population dispersion in the absence of a chemical gradient.Using the SFDC assay and an individual-cell-based mathematical model, we successfully determined values for both of these population parameters for Escherichia coli K12 responding to fucose. The values obtained were μ = 1.1 ± 0. 4 × 10-5 cm2/s and χo = 8 ± 3 ± 10-5 cm2/s. We have demonstrated a method capable of determining these parameter values from the now validated mathematical model which will be useful for predicting bacterial migration in application systems.
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  • 94
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    Biotechnology and Bioengineering 38 (1991), S. 296-303 
    ISSN: 0006-3592
    Keywords: ethanol ; genetic engineering ; Escherichia coli ; lignocellulose ; xylose ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: The conversion of xylose to ethanol by recombinant Escherichia coli has been investigated in pH-controlled batch fermentations. Chemical and environmental parameters were varied to determine tolerance and to define optimal conditions. Relatively high concentrations of ethanol (56 g/L) were produced from xylose with excellent efficiencies. Volumetric productivities of up to 1.4 g ethanol/L h were obtained. Productivities, yields, and final ethanol concentrations achieved from xylose with recombinant E. coli exceeded the reported values with other organisms. In addition to xylose, all other sugar constituents of biomass (glucose, mannose, arabinose, and galactose) were efficiently converted to ethanol by recombinant E. coli. Unusually low inocula equivalent to 0.033 mg of dry cell weight/L were adequate for batch fermentations. The addition of small amounts of calcium, magnesium, and ferrous ions stimulated fermentation. The inhibitory effects of toxic compounds (salts, furfural, and acetate) which are present in hemicellulose hydrolysates were also examined.
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  • 95
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    Biotechnology and Bioengineering 39 (1992), S. 732-740 
    ISSN: 0006-3592
    Keywords: cell disruption ; chemical permeabilization ; Escherichia coli ; fermentation ; protein recovery ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Overall protein release greater than 75% in less than 1 h can be attained by exposing exponentially growing Escherichia coli cells to 0.4 M guanidine plus 0.5% Triton X-100 at 37°C in medium. Cell growth stops immediately upon addition of the chemicals, but the cells are not lysed. Guanidine concentrations lower than 0.2 M, in conjunction with 0.5% Triton X-100, do not release significant intracellular protein, nor do they inhibit cell growth. Under these conditions, the cells undergo an adaptation that confers resistance to protein release by further treatment with guanidine and Triton X-100. Cells treated with 0.2 M guanidine plus 0.5% Triton X-100 display intermediate behavior. Protein release is approximately 35%, and growth is temporarily interrupted by an extended lag phase. Subsequent resumption of cell growth results in resistant cells and no additional protein release. This resistance is shown to be reversible and is most likely due to physiological adaptation rather than genetic mutation.
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  • 96
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    Biotechnology and Bioengineering 40 (1992), S. 1197-1202 
    ISSN: 0006-3592
    Keywords: Escherichia coli ; plasmid retention ; amino acid supplementation ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: The effect of amino acid supplementation on plasmid stability in Escherichia coli B/r was tested experimentally. Comparisons of experimental results to computer-predicted values were made using a detailed, structured single-cell model. The plasmid, pDW17 (a pBR322 derivative with a mutated tac promoter controlling the β-lactamase gene), was used. In chemostat cultures, the amino acid supplemented cultures were always less stable than those grown in minimal medium. This effect was not a growth rate effect, as increasing growth rate imsproves stability for both cultures in minimal medium and in amino acid supplemented medium. The computer model also predicted a decrease in stability due to amino acid supplementation. The model also predicts that amino acid supplementation, combined with moderately strong plasmid-encoded protein expresion, results in a depletion of low-molecular-weight organics compared with plasmid-free cells. In minimal medium the same level of plasmid-encoded protein synthesis results in a strong reduction in amino acid pools compared with plasmid-free cells. With amino acid supplementation the growth differential between plasmid-bearing and plasmid-free cells may be due to an “energy limitation,” while in minimal medium the size of the growth rate differential may be due to a “building block” limitation. © 1992 John Wiley & Sons, Inc.
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  • 97
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    Biotechnology and Bioengineering 41 (1993), S. 395-404 
    ISSN: 0006-3592
    Keywords: recombinant bacterium ; plasmid loss ; modeling ; Escherichia coli ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: A large number of models concerning cultures of genetically engineered bacteria have been described. Among them, some are specifically adapted to continuous cultures and lead to the determination of two variables: (i) the difference in the specific growth rates between plasmid-carrying cell and plasmid-free cells (δμ) and (ii) the frequency of plasmid loss by plasmid-containing cells (prμ+). Until now, studies have been performed on the global expression prμ+ and δμ, whose value during continuous assays have been supposed approximately constant (mean value) and not on separate values of both terms pr and μ+, respectively, probability of plasmid loss and specific growth rate of the plasmid-carrying cells. So far these studies do not allow examination of the relationship between these two last parameters. Experimental results were obtained with Escherichia coli C600 galk (GAPDH), a genetically engineered strain that synthetizes an elevated quantity of glyceraldehyde-3-phosphate dehydrogenase (GAPDH). From data obtained during continuous cultures, it is shown that during an assay, δμ, and prμ+ do not remain constant. An appropriate mathematical analysis of the expression of μ- (specific growth rate of the plasmid-free cells) and μ+ has been built up. This allows the evaluation of the values of μ+ and μ- during the continuous cultures carried out at different dilution rates. Values of pr have been calculated from these data. Indeed our results show that pr increases with μ+. A modeling approach which allows correct simulation of this variation is also proposed. This model is derived from the Hill equation regarding cooperative binding of enzymic type reaction. © 1993 John Wiley & Sons, Inc.
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  • 98
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    Biotechnology and Bioengineering 41 (1993), S. 666-670 
    ISSN: 0006-3592
    Keywords: oxygen fluctuations ; plasmid amplification ; Escherichia coli ; circulation time distribution ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Escherichia coli DH5α, carrying the pUC19 plasmid for the lacZ fragment of β-galactosidase and ampicillin resistance, was grown in a batch fermentor under conditions of fluctuating oxygen supply. A Monte Carlo method was used to control the on/off supply of air to simulate circulation of cells in a large fermentor. Rapid changes in oxygen supply reduced the rates of oxygen uptake the carbon dioxide release and prolonged the active second growth phase in batch culture, compared to growth with continuous aeration. Amplification of the plasmid was observed during the stationary phase when air supplied continuously, but not during the Monte Carlo experiments. © 1993 John Wiley & Sons, Inc.
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  • 99
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    Biotechnology and Bioengineering 41 (1993), S. 781-790 
    ISSN: 0006-3592
    Keywords: Escherichia coli ; recombinant ; fed batch ; high cell density ; trypsin ; fermention ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Fed-batch techniques were employed to obtain high cell density cultures (92-100 g DCW/L) of Escherichia coli strain X90 producing a recombinant serine protease, rat anionic trypsin, secreted to the periplasm. The specific growth rate was controlled to minimize growth-inhibiting acetate formation by utilizing an exponential feeding profile determined from mass balance equation. The volumetric yield of recombinant rat anionic trypsin was 56 mg/L, and the final cell density was 92 g DCW/L when the culture was induced in the late logarithmic phase. However, when the culture was induced in the early logarithmic phase, the volumetric yield was 13 mg/L and the final cell density was 14 g DCW/L. Thus, the induction timing is shown to have a significant effect on the final cell density as well as the overall volumetric yield of the recombinant protease. © 1993 Wiley & Sons, Inc.
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  • 100
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    Biotechnology and Bioengineering 42 (1993), S. 30-36 
    ISSN: 0006-3592
    Keywords: Escherichia coli ; fiber optic ; firefly luciferase ; on-line ; viability ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: A novel method is described for the on-line determination of viable cell number. It has been tested in fermentations of Escherichia coli. The cells are transfected with the gene for firefly luciferase and fed low levels of luciferin in the medium. The reaction requires ATP, so the nonviable cells cannot produce light. Thus, light production is linear with viable cell density from innoculation through most of exponential growth. The light emitted by these cells is then conducted from the reaction vessel to the light detection equipment by an optical fiber. With the equipment described below, as few as a 106 cells/mL, or an OD600 of 0.004, are easily detectable and concentrations greater than 1010 cells/mL are well within range. The data are collected by a computer, so adaptation to on-line control applications is straightforward. During lag phase, this method is much more accurate then optical density measurements. At the end of exponential growth, rapid changes in light production mark carbon source depletion and the onset of cell lysis. A simple model accounts for the luciferin used during the fermentation and corrects the light detected to the proper cell density. © 1993 John Wiley & Sons, Inc.
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