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E Keshavarz-Moore

Publications and source records attributed to E Keshavarz-Moore.

11 recordsLinked to original sources
PubMed2002

Ultra scaledown to predict filtering centrifugation of secreted antibody fragments from fungal broth.

Extracellularly expressed anti-hen egg lysozyme single-chain antibody fragments (scFv) produced by Aspergillus awamori were recovered using filtering centrifugation. Two filtering centrifuges with 0.5- and 30-L capacities were used to represent laboratory- and pilot-scale equipment, respectively. Critical regime analysis using the computational fluid dynamics (CFD) technique provided information about the local energy dissipation rates in both units. Experimental data indicated loss of scFv activity for energy dissipation rates above about 2.0 x 10(4) W kg(-1). This loss of activity increased in the presence of gas-liquid interfaces during filtering centrifugation. An ultra scaledown filtering centrifuge with a maximum working volume of 35 mL was designed to mimic the operating conditions identified by the critical regime analysis for the laboratory- and pilot-plant-scale units. The recovered scFv activity levels and the separation performance of the three units were comparable when operated at equal maximum energy dissipation rates.

Animals↗
PubMed2002

A comparison of the process issues in expressing the same recombinant enzyme periplasmically in Escherichia coli and extracellularly in Streptomyces lividans.

The choice of a host for the production of a biological molecule will have a significant effect on isolation and purification procedures employed. This paper makes a comparison between the production of a single enzyme, a recombinant alpha-amylase, in Escherichia coli and Streptomyces lividans, on a small scale. It defines the differences in the cultivation and in the isolation stages and also describes the impact of the expression system on later downstream processing steps. At the cultivation stage, the specific productivity of the E. coli in units per gram per hour is four times that of the S. lividans while the total biomass yields are of the same order. The initial volume for downstream processing of S. lividans is six-fold larger and the total protein released into the extracellular medium is three times greater than E. coli, however, the recoverable yield from the E. coli is a fifth of that obtained from the S. lividans and requires three additional stages prior to chromatography. Even with these stages the final specific activity is 64% of the S. lividans. The results indicate the need to consider the whole process when making such comparisons.

Biomass↗
PubMed2002

Disruption of leaves and initial extraction of wildtype CPMV virus as a basis for producing vaccines from plants.

Wildtype cowpea mosaic virus (CPMV) was extracted from fresh and frozen plant material by methods suitable for large-scale application. Deep freezing, crushing, and thawing in water or buffers gave 0.6+/-0.2 mg g(-1) of virus after up to 24 h. Release from sliced fresh leaves was lower at 0.14+/-0.03 mg g(-1). Homogenisation of frozen leaves for 1 min increased yield to a maximum, on average of 3.5 mg g(-1) but varying between batches from 2.2 to 4.8 mg g(-1) virus Long term storage at -80 degrees C increased subsequent yield by 2 mg g(-1) per year on average; the maximum was 10.4+/-1.9 mg g(-1) (665 days storage). Within a batch, similar yields were obtained between individual fresh plants, and from frozen versus fresh leaves. After homogenisation for 1 min, 90% of debris particles were smaller than 12 microm, half under 5 microm and 10% less than 1 microm. Homogenate (4% dry weight) was rheologically complex, exhibiting shear thinning with hysteresis at low shear rates which bears on subsequent processing. At shear rates above 200 s(-1), its apparent viscosity was 0.02 N s m(-2).

Biotechnology↗
PubMed2000

Effects of growth medium selection on plasmid DNA production and initial processing steps.

Cultures of recombinant Escherichia coli containing the plasmid pSVbeta were grown in three medium formulations to assess their effects on the characteristics of supercoiled plasmid DNA production for plasmid-based gene therapy. A semi-defined medium containing casamino acids (SDCAS) was found to support higher cell densities and higher plasmid stability than a similar medium containing soya amino acids (SDSOY) or Luria-Bertani medium (LB). Differences were observed in the cell harvest characteristics, plasmid DNA primary recovery, plasmid DNA yield and quality between cells grown on LB and on SDCAS medium. Cells grown on SDCAS medium were more difficult to resuspend after harvest than those grown in LB medium and were less susceptible to alkaline lysis. The plasmid DNA content from SDCAS was predominantly supercoiled and was less contaminated by chromosomal DNA than plasmid DNA extracts derived from cells grown on LB medium. It was hypothesised that the different carbon:nitrogen ratio (C:N) of the medium may have been responsible for changing the cell wall polysaccharide composition resulting in the change in cell harvest and lysis characteristics. Results indicated that changing the C:N ratio of SDCAS medium between 1.21:1 and 12.08:1 resulted in no alteration in cell wall polysaccharide composition or in cell susceptibility to chemical lysis or physical breakage. Plasmid DNA yields increased ten-fold with ten-fold increase in the C:N ratio of SDCAS medium.

Biotechnology↗
PubMed1999

Rapid quantitation and monitoring of plasmid DNA using an ultrasensitive DNA-binding dye.

A sensitive fluorescence-based method for monitoring plasmid DNA during production was investigated. This simple method of assaying for plasmid DNA allows rapid monitoring of plasmid yields from a recombinant Escherichia coli fed-batch fermentation. The assay has several advantages over traditional methods of plasmid DNA measurement. The fluorescent dye is highly specific and can measure total plasmid DNA concentration in about 5 min. The assay is sensitive over a wide range of plasmid concentrations of between 15 and 280 ng/mL, even in the presence of impurities that occur within alkaline lysate preparations. The technique can also be applied to monitoring fermentation and downstream purification steps.

Biotechnology↗
PubMed1997

Factors determining more efficient large-scale release of a periplasmic enzyme from E. coli using lysozyme.

Large scale use of lysozyme for periplasmic release has been impeded by the cost of the pure enzyme and its subsequent presence as a contaminant in later downstream processing steps. In this paper, we discuss the use of lysozyme for pilot scale recovery of a periplasmic enzyme from E. coli. The effects of concentration of sucrose, lysozyme and cells on periplasmic enzyme release were examined. Lysozyme concentration can be reduced 5-fold from previous reports and a reduction in sucrose concentration from 20 to 15% (w/v) allows an improvement in centrifugal harvesting by reducing viscosity. High levels of release were still achieved using this technique and further improvements in yield were obtained by optimising other components of the releasing mixture. Results show that some release is still achieved in circumstances where no lysozyme use is possible. Results also indicate that a substantial proportion (up to 70%) of lysozyme remains bound to the cellular debris after its action and is removed with this material.

Escherichia coli↗
PubMed1996

Production of cadmium sulphide microcrystallites in batch cultivation by Schizosaccharomyces pombe.

Cadmium sulphate was added to separate batch cultures of Schizosaccharomyces pombe during different growth phases to determine the effect on cadmium sulphide microcrystallite production. Exit gas analysis was used to determine the impact on metabolism. Addition during the early-exponential growth phase resulted in an immediate intracellular uptake of cadmium, followed by rapid efflux from the cells, permanent reduction in cell metabolism and a lower intracellular inorganic sulphide content. This response was not suitable for cadmium sulphide microcrystallite production. Stationary phase cultures did not induce cadmium sulphide microcrystallite production. However, the addition of cadmium sulphate to a culture during the mid-exponential growth phase increased the intracellular cadmium and inorganic sulphide concentrations for approximately 8 h before reaching a saturation level for the cell. This resulted in a significant level of cadmium sulphide microcrystallite production.

Biological Transport, Active↗
PubMedDate not supplied

Factors affecting the production of a single-chain antibody fragment by Aspergillus awamori in a stirred tank reactor.

A recombinant strain of Aspergillus awamori expressing anti-lysozyme single chain antibody fragments (scFv), under the control of a xylanase promoter, was studied in order to investigate the impact of medium, induction regime and protease production on the expression of the product. Experiments with the time of induction showed that the optimum results are achieved when induction is started in the late exponential phase (21 h after inoculation) improving the titer of the product from 14.5 mg L(-1), obtained in the early exponential phase (7 h after inoculation), to 16.2 mg L(-1). A 100% increase of the carbon (fructose) and nitrogen (ammonium sulfate) sources in the growth medium resulted in an increase in product concentration from 16.2 to 108.9 mg L(-1) and an increase in maximum dry cell weight from 7.5 to 11.5 g L(-1). A 50% reduction in the concentration of the inducer resulted in an increase in the product yield from 10 mg g(-1) dry cell weight to 12 mg g(-1). Proteolytic enzymes were produced during the fermentation up to concentrations equivalent to 1.4 g L(-1) trypsin, but they had no detrimental effect on the concentration of the antibody fragment.

Aspergillus↗