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- Liu, Yanling, 1974-
(författare)
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Electric DNA chips for determination of pathogenic microorganisms
- 2008
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Doktorsavhandling (övrigt vetenskapligt/konstnärligt)abstract
- Silicon-based electric DNA chip arrays were utilized to fast identify pathogenic microorganisms with respect to the capacity to produce toxins involved in foodborne poisoning and infections. Bacteria of the B. cereus and the enterohemorrhagic E. coli (EHEC) groups contain different set-ups of various virulence factors that are encoded by the corresponding genes. The purpose of this work was to develop a fast and simple method for determination of the presence of these virulence genes in a colony from primary enrichment cultures. A target gene is detected through hybridization to a surface-immobilized specific capture probe and biotin-labeled detection probe. Following binding of an enzyme conjugate to this sandwich hybrid complex, a current signal is generated by electronic redox recycling of the enzymatic product paminophenol (pAP). Two versions of the assay were developed. In the first version the capture probes were immobilized on magnetic beads, which carried out all reactions until the pAP generation, while the final electric signal was created by transferring pAP to a single-electrode chip surface. In the second version a silicon chip array with 16 parallel sensing electrode positions each of them functionalized by capture probes, carried out all assay steps on the chip surface. This instrument can realize automatic and multiplexed gene detection. The kinetics of bacterial cell disruption and impact of DNA fragmentation by ultrasound were determined. The experimental data suggested that the increased signal after first minutes of ultrasonication were due to the accumulation of released DNA amount, while the further signal increase resulted from the improved hybridization with the shortened target DNA strands. Studies on probe localization on the 16-electrode chip assays indicated that the probe-targeting site, which was located at the 5’-end of strands, gave rise to the highest signal level due to the efficient targetprobes hybridization and the following enzyme binding. When these functionalized chip arrays were exposed to the cell homogenates, the sensing electrodes were fouled by cellular proteins and therefore led to dramatically decreased redox-recycling current. To circumvent this, samples were treated by DNA extraction after the 1st sonication and then DNA fragmentation by a 2nd time sonication. The DNA extract removed most of the interfering components from bacterial cell. This sample treatment was applied to characterize one “diarrheal” and one “emetic” strain of B. cereus with the chip arrays functionalized by eight DNA probes. The signal patterns of eight virulence genes from chip assays agreed well with PCR control analyses for both strains. By simply adding the SDS detergent to cell homogenates, chip surface blocking effect can be significantly reduced even without DNA extraction treatment. After optimization of some critical factors, the 16-electrode DNA chips with the improved sensing performance can directly detect multiple virulence genes from a single E. coli colony in 25 min after the introduction of supernatant of ultrasonicated cell lysate.
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| 3. |
- Sundström, Heléne, 1962-
(författare)
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Analytical tools for monitoring and control of fermentation processes
- 2007
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Doktorsavhandling (övrigt vetenskapligt/konstnärligt)abstract
- The overall objective of this work has been to adopt new developments and techniques in the area of measurement, modelling and control of fermentation processes. Flow cytometry and software sensors are techniques which were considered ready for application and the focus was set on developing tools for research aiming at understanding the relationship between measured variables and process quality parameters. In this study fed-batch cultivations have been performed with two different strains of Escherichia coli (E.coli) K12 W3110 with and without a gene for the recombinant protein promegapoietin. Inclusion body formation was followed during the process with flow cytometric detection by labelling the inclusion bodies with first an antibody against the protein promegapoietin and then a second fluorescent anti-antibody. The approach to label inclusion bodies directly in disintegrated and diluted cell slurry could be adopted as a method to follow protein production during the process, although the labelling procedure with incubation times and washings was somewhat time-consuming (1.5 h). The labelling of inclusion bodies inside the cells to follow protein production was feasible to perform, although an unexplained decrease in the relative fluorescence intensity occurred late in process. However, it is difficult to translate this qualitative measurement into a quantitative one, since a quantitative protein analysis should give data proportional to the volume, while the labelling of the spheric inclusion bodies gives a signal corresponding to the area of the body, and calibration is not possible. The methods were shown to be useful for monitoring inclusion body formation, but it seems difficult to get quantitative information from the analysis. Population heterogeneity analysis was performed, by using flow cytometry, on a cell population, which lost 80-90% viability according to viable count analysis. It was possible to show that the apparent cell death was due to cells incapable of dividing on agar plates after induction. These cells continued to produce the induced recombinant protein. It was shown that almost all cells in the population (≈97%) contained PMP, and furthermore total protein analysis of the medium indicated that only about 1% of the population had lysed. This confirms that the "non-viable" cells according to viable count by cfu analysis produced product. The software sensors XNH3 and µNH3, which utilises base titration data to estimate biomass and specific growth rate was shown to correlate well with the off-line analyses during cultivation of E. coli W3110 using minimal medium. In rich medium the µNH3 sensor was shown to give a signal that may be used as a fingerprint of the process, at least from the time of induction. The software sensor KLaC* was shown to respond to foaming in culture that probably was caused by increased air bubble dispersion. The RO/S coefficient, which describes the oxygen to substrate consumption, was shown to give a distinct response to stress caused by lowered pH and addition of the inducing agent IPTG. The software sensor for biomass was applied to a highly automated 6-unit multi-bioreactor system intended for fast process development. In this way also specific rates of substrate and oxygen consumption became available without manual sampling.
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| 4. |
- Svensson, Marie, 1972-
(författare)
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The temperature-limited fed-batch technique for control of Escherichia coli cultures
- 2006
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Doktorsavhandling (övrigt vetenskapligt/konstnärligt)abstract
- The objective of this study was to investigate the physiology and productivity in Escherichia colicultures with emphasis on the temperature-limited fed-batch (TLFB) culture. The TLFB techniquecontrols the oxygen consumption rate of the growing culture by a gradually declining temperaturefrom 37-35 °C down to 20-18 °C. The temperature regulated the DOT around a set-point (30 % airsat.), and all nutrients were in excess. Glucose was fed into the culture continuously, however, highacetate formation was avoided by keeping the glucose at a low, yet excessive, concentration. Thebiomass productivity was approximately the same in TLFB as in glucose-limited fed-batch (GLFB)cultures, since the specific growth rate and the oxygen consumption rate are limited by the oxygentransfer capacity of the reactor in both techniques.High concentrations of endotoxins were found in the medium of E. coli fed-batch cultures at lowspecific growth rates (below 0.1 h-1) and severe glucose limitation. In this thesis the TLFB techniquewas found to suppress the endotoxin release even at low specific growth rates. The repressed release of endotoxins in TLFB cultures was due to the high availability of glucose and not to the low growthrate or the lower temperature. The conclusion was drawn from comparing with the GLFB technique performed at 20 °C, which resulted in high endotoxin release.Extensive release of endotoxin, accompanied with high concentrations of soluble proteins was foundin a TLFB culture exposed to a higher energy dissipation rate, 16 kW m-3, instead of 2 kW m-3, due toa higher stirrer speed (1000 instead of 500 rpm). The hypothesis that this is a result of mechanicalstress is discussed in context with the common view that cells like E. coli, which are smaller than the Kolmogoroff’s microscale of turbulence, should not be influenced by the turbulence.TLFB cultured cells exhibited more stable cytoplasmic membranes when treated with osmotic shockas compared to the GLFB cultured cells. The concentrations of DNA and soluble proteins in the periplasmic extracts from the TLFB cultured cells were lower than from GLFB cultured cells. Inaddition, the specific productivity of periplasmic β-lactamase was higher in the TLFB cultures,suggesting that this technique could be an alternative for protein production. The solubility of apartially aggregated recombinant protein increased in the TLFB compared to the GLFB cultures.However some time after induction, in spite of the gradually declining temperature, the solublefraction decreased.For obtaining better understanding of the performance of the process and for identifying criticalparameters, a mathematical model was developed based on the growth, energy and overflowmetabolism at non-limiting nutrient conditions. The temperature-dependent maximum specific glucoseand oxygen uptake rates were determined in pH-auxostat cultures for temperatures ranging from 18 to37 °C. A dynamic simulation model of the TLFB technique was developed and the results were compared to experimental data. The simulation program was also used for sensitivity analysis of some physiological and process parameters to study the impact on biomass concentration and temperatureprofiles. An effect on the biomass concentration profile but not on the temperature profile wasobserved when changing the oxygen transfer coefficient. If the maximum specific glucose uptake ratewas altered, or if the glucose concentration was permitted to assume other values, the temperatureprofile but not the biomass concentration profile was influenced. Cell death affected both the biomassconcentration profile and the temperature profile.
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