M.P. Nandakumar
Lund University
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Featured researches published by M.P. Nandakumar.
Biosensors and Bioelectronics | 2000
R Nandakumar; M.P. Nandakumar; Bo Mattiasson
A monoclonal-antibody-based, sequential competitive-flow-injection immunoassay system in expanded-bed mode has been developed for the determination of nisin. The system allows the determination of nisin in the presence of suspended particles without any significant interference, illustrating its potential for on-line monitoring of fermentation processes or the analysis of food matrices. The dose response range of the system when operated in expanded-bed mode was 6-90 microM. The detection limit under packed-bed conditions was 3 microM. The results correlated well with the results from conventional ELISA in the analysis of samples of processed cheese. When milk samples, fermentation samples and buffer were spiked with nisin, the mean recoveries were 86% for milk samples, 96% for fermentation samples and 98% for buffer solution.
Bioseparation | 1999
Bo Mattiasson; M.P. Nandakumar
Competitive binding assays have been performed in flow injection systems. To further increase the versatility of the system, and to enable it to deal with samples containing particulate matter, the adsorption step was designed as an expanded bed column. Immunochemical quantification of human serum albumin was chosen as a model system to use for the development of the technology. A competitive ELISA was set up using peroxidase labelled HSA as competing ligand. The introduction of the expanded bed immunosorption column made the system tolerant to samples containing suspended particulate matter. The analytical outcome is very similar to that from the packed bed system even though more time is required for each assay cycle. The capability of the system was tested by addition of increasing amounts of yeast cells. The results clearly indicate that the system is suitable e.g. for process monitoring of fermentations.
Bioseparation | 1999
M.P. Nandakumar; Arvind Lali; Bo Mattiasson
A novel flow injection biosensor system for monitoring fermentation processes has been developed using an expanded micro bed as the enzyme reactor. An expanded bed reactor is capable of handling a mobile phase containing suspended matter like cells and cell debris. Thus, while the analyte is free to interact with the adsorbent, the suspended particulate matter passes through unhindered. With the use of a scaled down expanded bed in the flow injection analysis (FIA) system, it was possible to analyse samples directly from a fermentor without the pretreatment otherwise required to extract the analyte or remove the suspended cells. This technique, therefore, provides a means to determine the true concentrations of the metabolites in a fermentor, with more ease than possible with other techniques.Glucose oxidase immobilised on STREAMLINE was used to measure glucose concentration in a suspension of dead yeast cells. There was no interference from the cell particles even at high cell densities such as 15 gm dry weight per litre. The assay time was about 6 min. Accuracy and reproducibility of the system was found to be good. In another scheme, lactate oxidase was covalently coupled to STREAMLINE for expanded bed operation. With the on-line expanded micro bed FIA it was possible to follow the fermentation with Lactobacillus casei.
Applied Microbiology and Biotechnology | 1999
M.P. Nandakumar; A. Sapre; Arvind Lali; Bo Mattiasson
Abstract A highly sensitive glucose sensor, operating in flow-injection analysis (FIA) mode, was developed for the detection of glucose in fermentation broth. The assay system is based upon the post-column reaction of the peroxide formed in the glucose-oxidase-catalysed reaction and subsequent spectrophotometric detection of the coloured product formed. The sensor system was characterised and calibrated using standard solutions, and later used for quantification of glucose in fermentation media. Two types of enzyme column were used: one operated in packed-bed mode and the other in expanded- bed mode. Both columns were integrated into a FIA system and were found to give good analytical results. Glucose concentrations as low as 0.1 mg/l and 5 mg/l could be detected in packed- and expanded-bed modes respectively. Glucose concentrations were measured during typical fed-batch fermentation conditions in this system, and the results are presented.
Biotechnology Letters | 2001
T. Mugochi; M.P. Nandakumar; Remigio Zvauya; Bo Mattiasson
A bioassay for the rapid detection of bacteriocins by detecting efflux of K+ ions from a bacteriocin-sensitive indicator strain was developed. There was a rapid increase in concentration of K+ in the medium from approximately 1.6 to 9.5 mM when the crude bacteriocin was added to the sensitive strain. A bacteriocin activity of 8.25 AU ml−1 produced the lowest detectable concentration of K+ (0.179 mM) and the smallest inhibition zone (0.4 mm). The smallest cell dry mass of the indicator strain capable of releasing a detectable level of K+ (0.102 mM) was 0.76 mg. Detection of the bacteriocin by measuring the efflux of K+ compares well with the conventional agar well diffusion assay. Low activities of bacteriocin and low amounts of the sensitive indicator strain biomass can be used with this bioassay.
Bioseparation | 1999
M.P. Nandakumar; Anita Tocaj; Bo Mattiasson
A method for cell disruption in Flow Injection Analysis (FIA) systems has been developed. The principle involves on-line cell disruption by means of immobilised lysozyme followed by an ultrasonic treatment. In order to avoid flow problems in the analytical system, the lysozyme was immobilised to Streamlinereg that was used in an expanded bed in the flow system. Samples of suspensions of Micrococcus lysodeikticus were treated and the success of the treatment was evaluated in terms of released protein and as a decrease in the optical density at 450 nm. The new technology offers a powerful tool in flow injection analyses for quantification of intracellular compounds. The concept of integration, i.e. combining cell disruption with handling of cell debris and assay procedure in one continuous flow process facilitates its use and increases the probability of reaching reproducible and reliable results.
Biosensors and Bioelectronics | 2001
A. Collins; M.P. Nandakumar; Elisabeth Csöregi; Bo Mattiasson
Abstract A bienzyme flow injection system is presented for the monitoring of α-ketoglutarate produced in a fermentation process, using glutamate dehydrogenase (GDH) and glutamate oxidase (GlOx) immobilised in two serially connected expanded bed reactors. The use of expanded bed resulted in unhindered passage of the bacterial cells through the columns, and thereby the need of a separate filtering step (e.g. microdialysis) was avoided. In the first reactor, α-ketoglutarate was converted to l -glutamate by GDH in the presence of ammonia and NADH. In the following reactor, l -glutamate was converted by GlOx to α-ketoglutarate, ammonia and hydrogen peroxide, which was detected in an electrochemical flow-through cell at +650 mV vs. Pt/(0.1 M KCl). The detection limit of α-ketoglutarate in the coupled packed bed reactors was 1 μM (defined as 3 S/N), the linear range 0–100 μM, and the sensitivity 0.80 nA/μM (R2 0.99). In the coupled expanded bed reactors, the detection limit of α-ketoglutarate was 7 μM (defined as 3 S/N), the linear range and the sensitivity being 0–500 μM and 0.11 nA/μM (R2 1.00), respectively. The response time (defined as the time between peak rise and return to baseline) was 5 min for coupled packed beds (injection of supernatant), and 12 min for coupled expanded beds (injection of sample containing cellular and particulate matter). Several other parameters, such as reactor stability, flow rate dependency, bed expansion, glutamate interference, etc. were investigated and characterised. When analysing real samples from a fermentation broth, the same results were obtained independent of the nature of the reactor system (packed or expanded bed). The hereby described system can easily be automatised and controlled from a personal computer.
Bioseparation | 1999
Anita Tocaj; M.P. Nandakumar; Olle Holst; Bo Mattiasson
A continuous integrated process for on-line quantification of intracellular components has been developed. By applying the concept of expanded micro-beds in a flow injection system it was possible to first perform on-line cell disintegration followed by an on-line binding assay for quantification of a reporter protein (beta-galactosidase) from the cell interior. The disintegration process involved the use of an expanded bed with immobilised lysozyme followed by ultrasonic treatment in a flow-through cell. The cell debris does not interfere in the binding assay as it is carried out in an expanded bed. The time for an assay cycle is at present approx. 35 min. This integrated system can be used for quantification of proteins down to at least 10(-7) mol/L.
Biotechnology Letters | 2001
M.P. Nandakumar; E. Nordberg Karlsson; Bo Mattiasson
An integrated flow injection process for analysis of intracellular components of microbes has been used to monitor plasmid content in Escherichia coli cultivations inoculated with cells subcultured in the presence or absence of ampicillin. The system allows sampling, sample handling, cell disruption, separation of intracellular components, and analysis in a semi-on-line mode of operation. The time scale for the assay is in the range 15 min (plasmid peak) to 25 min (complete assay cycle). As expected, lower initial plasmid content was found using an inoculum subcultured in the absence of ampicillin. More importantly, significant decrease in plasmid content was detected in the later stages of the cultivations (grown in ampicillin containing medium) even when using inoculum subcultured in the presence of ampicillin. This illustrates the versatility of the system, which allows monitoring of plasmid content as the cultivation proceeds.
Biotechnology Techniques | 1999
M.P. Nandakumar; Bo Mattiasson
Immobilised metal chelate affinity chromatography (IMAC) in an expanded bed mode was used for the purification of horse radish peroxidase. Recovery of horse radish peroxidase varied between 85 and 72% starting from the crude homogenate. When a pure peroxidase was passed through the purification protocol a recovery of about 95% was achieved.