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  • 1
    Electronic Resource
    Electronic Resource
    Oxford, UK : Blackwell Publishing Ltd
    Contact dermatitis 12 (1985), S. 0 
    ISSN: 1600-0536
    Source: Blackwell Publishing Journal Backfiles 1879-2005
    Topics: Medicine
    Type of Medium: Electronic Resource
    Location Call Number Limitation Availability
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  • 2
    Electronic Resource
    Electronic Resource
    Oxford, UK : Blackwell Publishing Ltd
    Annals of the New York Academy of Sciences 413 (1983), S. 0 
    ISSN: 1749-6632
    Source: Blackwell Publishing Journal Backfiles 1879-2005
    Topics: Natural Sciences in General
    Type of Medium: Electronic Resource
    Location Call Number Limitation Availability
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  • 3
    Electronic Resource
    Electronic Resource
    Oxford, UK : Blackwell Publishing Ltd
    Annals of the New York Academy of Sciences 434 (1984), S. 0 
    ISSN: 1749-6632
    Source: Blackwell Publishing Journal Backfiles 1879-2005
    Topics: Natural Sciences in General
    Type of Medium: Electronic Resource
    Location Call Number Limitation Availability
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  • 4
    Electronic Resource
    Electronic Resource
    Springer
    Bioprocess and biosystems engineering 15 (1996), S. 265-273 
    ISSN: 1432-0797
    Source: Springer Online Journal Archives 1860-2000
    Topics: Process Engineering, Biotechnology, Nutrition Technology
    Notes: Abstract The comparative efficiencies of two special biocatalytic reactors designed to handle gel-like immobilized biocatalysts, the hollow tubes and the hollow zones reactors, have been assessed for the performance of the hydrolysis of benzylpenicillin to 6-aminopenicillanic acid and phenyl acetic acid by an immobilized penicillin amidase preparation. On the basis of the efficiency factor η15/35, representing the ratio of activity expressed in the reactor at the end of 15 minutes in relation to the activity loaded in the reactor, and on the conversion achieved at the end of a given time close to that required to attain conversions near those required in industrial operation the hollow tubes reactor revealed to be slightly superior to the hollow zones reactor. The application to the conversion data obtained in both reactors of the α, β kinetic model derived by Cardoso and Costa [1] also gave evidence of the superior performance of the hollow tubes reactor. The influence of the linear velocity on the final conversion achieved for the hollow tubes reactor was investigated allowing the conclusion that from a velocity across the reactor of at least about 17.6 cm min−1 the final conversion time is independent of this parameter. The application of the α, β kinetic model to the conversion data obtained in the hollow tubes reactor for different linear velocities also supported this conclusion. Although the kinetic behaviour of the conversion reaction for linear velocities higher than 17.6 cm min−1 varied with the linear velocity the final conversion was not affected by this parameter.
    Type of Medium: Electronic Resource
    Location Call Number Limitation Availability
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  • 5
    Electronic Resource
    Electronic Resource
    Springer
    Bioprocess and biosystems engineering 13 (1995), S. 215-221 
    ISSN: 1432-0797
    Source: Springer Online Journal Archives 1860-2000
    Topics: Process Engineering, Biotechnology, Nutrition Technology
    Notes: Abstract Experiments of ultrafiltration with diafiltration were performed on fermented broths of benzylpenicillin and clavulanic acid produced at pilot scale at CIPAN, SA to achieve solid/liquid separation, antibiotic recovery and soluble protein retention. This study was done using a laboratorial/pilot scale ultrafiltration facility from Paterson Candy International Ltd. whose modules have a tubular configuration. PVDF membranes with a molecular weight cut-off of 100 000 (FP10) and 200 000 (FP200) were assessed. Comparison between solvent extraction of benzylpenicillin and clavulanic acid from filtered broth and ultrafiltered broth was also done. It was concluded that ultrafiltration with diafiltration of fermented broths of antibiotics using the FP10 membrane is a valid alternative to the use of rotary vacuum filters, flocculants and filter aid, deserving a further study to establish the best operating conditions. An economic appraisal also seems to be of paramount importance.
    Type of Medium: Electronic Resource
    Location Call Number Limitation Availability
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  • 6
    Electronic Resource
    Electronic Resource
    Springer
    Bioprocess engineering 23 (2000), S. 191-197 
    ISSN: 0178-515X
    Source: Springer Online Journal Archives 1860-2000
    Topics: Process Engineering, Biotechnology, Nutrition Technology
    Notes: Abstract  Benzylpenicillin filtered broths purified by ultrafiltration and fermented broths clarified by ultrafiltration and afterwards concentrated by reverse osmosis were used directly for enzymatic conversion of benzylpenicillin to 6-aminopenicillanic acid and phenylacetic acid by immobilised penicillin G acylase or amidase. It was concluded that, when the ultrafiltration operation retained 100% of protein, the concentrates from reverse osmosis could be successfully directly fed to the enzymatic reactor, giving high enzymatic conversion yield of benzylpenicillin to 6-aminopenicillanic acid.
    Type of Medium: Electronic Resource
    Location Call Number Limitation Availability
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  • 7
    Electronic Resource
    Electronic Resource
    Springer
    Bioprocess engineering 21 (1999), S. 157-163 
    ISSN: 0178-515X
    Source: Springer Online Journal Archives 1860-2000
    Topics: Process Engineering, Biotechnology, Nutrition Technology
    Notes: Abstract Purification of benzylpenicillin filtered broths obtained from fermented broths produced at CIPAN, SA Pilot Plant Fermentation was carried out by ultrafiltration with diafiltration. This study was done using an ultrafiltration laboratory/pilot installation from Paterson Candy International Ltd. whose module has a tubular configuration. Membranes with molecular weight cut-offs of 8000 (polysulfone), 20 000 (polysulfone) and 100 000 (PVDF) were assessed. Comparison between solvent extraction of benzylpenicillin from ultrafiltered broths and from filtered broths using flocculants was also done. Ultrafiltration with diafiltration of benzylpenicillin filtered broths was used successfully to remove proteins, colored substances and other impurities giving high benzylpenicillin recovery in the permeate, as an alternative to the use of flocculants and anti-emulsion agents to obtain good phases separation in benzylpenicillin solvent extraction.
    Type of Medium: Electronic Resource
    Location Call Number Limitation Availability
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  • 8
    Electronic Resource
    Electronic Resource
    Springer
    Bioprocess engineering 22 (2000), S. 41-44 
    ISSN: 0178-515X
    Source: Springer Online Journal Archives 1860-2000
    Topics: Process Engineering, Biotechnology, Nutrition Technology
    Notes: Abstract Concentration of benzylpenicillin filtered broths purified by ultrafiltration and fermented broths clarified by ultrafiltration was carried out by reverse osmosis. This study was done using a reverse osmosis laboratory/pilot installation from Paterson Candy International Ltd. whose module has a tubular configuration and a membrane with a molecular weight cut-off of 100 Dalton (ZF99) made of a polyamide film with a rejection of 99% of NaCl. It was concluded that reverse osmosis is an adequate technique to concentrate benzylpenicillin ultrafiltered broths, leading to low losses of benzylpenicillin in the permeate and high benzylpenicillin recovery for high volumetric concentration factors.
    Type of Medium: Electronic Resource
    Location Call Number Limitation Availability
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  • 9
    Electronic Resource
    Electronic Resource
    Springer
    Bioprocess engineering 13 (1995), S. 215-221 
    ISSN: 0178-515X
    Source: Springer Online Journal Archives 1860-2000
    Topics: Process Engineering, Biotechnology, Nutrition Technology
    Notes: Abstract  Experiments of ultrafiltration with diafiltration were performed on fermented broths of benzylpenicillin and clavulanic acid produced at pilot scale at CIPAN, SA to achieve solid/liquid separation, antibiotic recovery and soluble protein retention. This study was done using a laboratorial/pilot scale ultrafiltration facility from Paterson Candy International Ltd. whose modules have a tubular configuration. PVDF membranes with a molecular weight cut-off of 100 000 (FP10) and 200 000 (FP200) were assessed. Comparison between solvent extraction of benzylpenicillin and clavulanic acid from filtered broth and ultrafiltered broth was also done. It was concluded that ultrafiltration with diafiltration of fermented broths of antibiotics using the FP10 membrane is a valid alternative to the use of rotary vacuum filters, flocculants and filter aid, deserving a further study to establish the best operating conditions. An economic appraisal also seems to be of paramount importance.
    Type of Medium: Electronic Resource
    Location Call Number Limitation Availability
    BibTip Others were also interested in ...
  • 10
    ISSN: 0178-515X
    Source: Springer Online Journal Archives 1860-2000
    Topics: Process Engineering, Biotechnology, Nutrition Technology
    Notes: Abstract  The comparative efficiencies of two special biocatalytic reactors designed to handle gel-like immobilized biocatalysts, the hollow tubes and the hollow zones reactors, have been assessed for the performance of the hydrolysis of benzylpenicillin to 6-aminopenicillanic acid and phenyl acetic acid by an immobilized penicillin amidase preparation. On the basis of the efficiency factor η15/35, representing the ratio of activity expressed in the reactor at the end of 15 minutes in relation to the activity loaded in the reactor, and on the conversion achieved at the end of a given time close to that required to attain conversions near those required in industrial operation the hollow tubes reactor revealed to be slightly superior to the hollow zones reactor. The application to the conversion data obtained in both reactors of the α, β kinetic model derived by Cardoso and Costa [1] also gave evidence of the superior performance of the hollow tubes reactor. The influence of the linear velocity on the final conversion achieved for the hollow tubes reactor was investigated allowing the conclusion that from a velocity across the reactor of at least about 17.6 cm min-1 the final conversion time is independent of this parameter. The application of the α, β kinetic model to the conversion data obtained in the hollow tubes reactor for different linear velocities also supported this conclusion. Although the kinetic behaviour of the conversion reaction for linear velocities higher than 17.6 cm min-1 varied with the linear velocity the final conversion was not affected by this parameter.
    Type of Medium: Electronic Resource
    Location Call Number Limitation Availability
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