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Volumn , Issue , 2006, Pages 1-383

Producing biomolecular substances with fermenters, bioreactors, and biomolecular synthesizers

(1)  Hochfeld, William L a  

a NONE

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EID: 85127955514     PISSN: None     EISSN: None     Source Type: Book    
DOI: None     Document Type: Book
Times cited : (9)

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    • Chisti, Y. and U.J.Jauregui-Haza, Biochem. Eng. J., 10, 143-153 (2002). Oxygen transfer and mixing in mechanically-agitated airlift bioreactors.
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    • Wenge, F., Y. Chisti, and M. Moo-Young, Chem. Eng. Comm., 155, 19-44 (1996). Split-cylinder airlift reactors: Hydraulics and hydrodynamics of a new mode of operation.
    • (1996) Chem. Eng. Comm , vol.155 , pp. 19-44
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    • Banerjee, U. C., Y. Chisti, and M. Moo-Young, Biotechnol. Tech., 7, 313-316 (1993). Spectrophotometric determination of mycelial biomass.
    • (1993) Biotechnol. Tech , vol.7 , pp. 313-316
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    • Chisti, Y. and M. Moo-Young, Trans. I. Chem. E., 74A, 575-583 (1996), Bioprocess intensification through bioreactor engineering.
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    • Automated fed-batch culture of recombinant Saccharomyces cerevisiae based on on-line monitored maximum substrate uptake rate.
    • Oh, G., M. Moo-Young, and Y. Chisti, Biochem. Eng. J., 1, 211-217 (1998). Automated fed-batch culture of recombinant Saccharomyces cerevisiae based on on-line monitored maximum substrate uptake rate.
    • (1998) Biochem. Eng. J , vol.1 , pp. 211-217
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    • A new method for the measurement of solids holdup in gas-liquid-solid three-phase systems.
    • Wenge, F., Y. Chisti, and M. Moo-Young, Ind. Eng. Chem. Res., 34, 928-935 (1995). A new method for the measurement of solids holdup in gas-liquid-solid three-phase systems.
    • (1995) Ind. Eng. Chem. Res , vol.34 , pp. 928-935
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    • Zhang, Z., M. Moo-Young, and Y. Chisti, Biotechnol. Adv., 14, 401-435 (1996). Plasmid stability in recombinant Saccharomyces cerevisiae.
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    • Biotransformations of rifamycins: Process possibilities.
    • Banerjee, U.C., B. Saxena, and Y. Chisti, Biotechnol. Adv., 10, 577-595 (1992). Biotransformations of rifamycins: Process possibilities.
    • (1992) Biotechnol. Adv , vol.10 , pp. 577-595
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    • Fed-batch production of baker's yeast using millet (Pennisetum typhoides) flour hydrolysate as the carbon source.
    • Ejiofor, A.O., Y. Chisti, and M. Moo-Young, J. Ind. Microbiol., 16, 102-109 (1996). Fed-batch production of baker's yeast using millet (Pennisetum typhoides) flour hydrolysate as the carbon source.
    • (1996) J. Ind. Microbiol , vol.16 , pp. 102-109
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    • Culture of Saccharomyces cerevisiae on hydrolysed waste cassava starch for production of baking-quality yeast.
    • Ejiofor, A.O., Y. Chisti, and M. Moo-Young, Enzyme Microb. Technol., 18, 519-525 (1996). Culture of Saccharomyces cerevisiae on hydrolysed waste cassava starch for production of baking-quality yeast.
    • (1996) Enzyme Microb. Technol , vol.18 , pp. 519-525
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    • Moo-Young, M., Y. Chisti, and D. Vlach, Biotechnol. Lett., 14, 863-868 (1992). Fermentative conversion of cellulosic substrates to microbial protein by Neurospora sitophila.
    • (1992) Biotechnol. Lett , vol.14 , pp. 863-868
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  • 250
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    • Production, purification, characterization, and applications of lipases.
    • Sharma, R., Y. Chisti, and U.C. Banerjee, Biotechnol. Adv., 19, 627-662 (2001). Production, purification, characterization, and applications of lipases.
    • (2001) Biotechnol. Adv , vol.19 , pp. 627-662
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  • 251
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    • Production and recovery of recombinant protease inhibitor alpha-1-antitrypsin.
    • Tamer, I.M. and Y. Chisti, Enzyme Microb. Tech., 29, 611-620 (2001). Production and recovery of recombinant protease inhibitor alpha-1-antitrypsin.
    • (2001) Enzyme Microb. Tech , vol.29 , pp. 611-620
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  • 252
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    • Fermentation optimization for the production of poly (beta-hydroxybutyric acid) microbial thermoplastic.
    • Grothe, E., M. Moo-Young, and Y. Chisti, Enzyme Microb. Tech., 25, 132-141 (1999). Fermentation optimization for the production of poly (beta-hydroxybutyric acid) microbial thermoplastic.
    • (1999) Enzyme Microb. Tech , vol.25 , pp. 132-141
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    • Optimization of poly (beta-hydroxybutyric acid) recovery from Alcaligenes latus: Combined mechanical and chemical treatments.
    • Tamer, I.M., M. Moo-Young, and Y. Chisti, Bioprocess Eng., 19, 459-468 (1998). Optimization of poly (beta-hydroxybutyric acid) recovery from Alcaligenes latus: Combined mechanical and chemical treatments.
    • (1998) Bioprocess Eng , vol.19 , pp. 459-468
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    • Disruption of Alcaligenes latus for recovery of poly (beta-hydroxybutyric acid): Comparison of high-pressure homogenization, bead milling, and chemically induced lysis.
    • Tamer, I.M., M. Moo-Young, and Y. Chisti, Ind. Eng. Chem. Res., 37, 1807-1814 (1998). Disruption of Alcaligenes latus for recovery of poly (beta-hydroxybutyric acid): Comparison of high-pressure homogenization, bead milling, and chemically induced lysis.
    • (1998) Ind. Eng. Chem. Res , vol.37 , pp. 1807-1814
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    • Fermentation (industrial): Basic considerations
    • Robinson, R., C. Batt, and P. Patel, eds., Academic Press, London
    • Chisti, Y., Fermentation (industrial): Basic considerations, in Encyclopedia of Food Microbiology, Robinson, R., C. Batt, and P. Patel, eds., Academic Press, London, 1999, pp. 663-674.
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    • Chisti, Y., Chem. Eng. Prog., 88(1), 55-58 (1992). Build better industrial bioreactors.
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    • Assure bioreactor sterility
    • Chisti, Y., Chem. Eng. Prog., 88(9), 80-85 (1992). Assure bioreactor sterility.
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    • Modern systems of plant cleaning
    • Robinson, R., C. Batt, and P. Patel, eds., Academic Press, London
    • Chisti, Y., Modern systems of plant cleaning, in Encyclopedia of Food Microbiology, Robinson, R., C. Batt, and P. Patel, eds., Academic Press, London, 1999, pp. 1806-1815.
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    • Fermentation technology, bioprocessing, scale up and manufacture
    • Moses, V., R.E. Cape, and D.G. Springham, eds., Harwood Academic Publishers, New York
    • Chisti, Y. and M. Moo-Young, Fermentation technology, bioprocessing, scale up and manufacture, in Biotechnology: The Science and the Business, second edition, Moses, V., R.E. Cape, and D.G. Springham, eds., Harwood Academic Publishers, New York, 1999, pp. 177-222.
    • (1999) Biotechnology: The Science and the Business, second edition , pp. 177-222
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    • Hydrodynamics and oxygen transfer in pneumatic bioreactor devices.
    • Chisti, Y. and M. Moo-Young, Biotechnol. Bioeng., 31, 487-494 (1988). Hydrodynamics and oxygen transfer in pneumatic bioreactor devices.
    • (1988) Biotechnol. Bioeng , vol.31 , pp. 487-494
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    • Liquid circulation in airlift reactors.
    • Chisti, Y., B. Halard, and M. Moo-Young, Chem. Eng. Sci., 43, 451-457 (1988). Liquid circulation in airlift reactors.
    • (1988) Chem. Eng. Sci , vol.43 , pp. 451-457
    • Chisti, Y.1    Halard, B.2    Moo-Young, M.3
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    • A reassessment of relationship between riser and downcomer gas holdups in airlift reactors.
    • Contreras, A., Y. Chisti, and E. Molina, Chem. Eng. Sci., 53, 41514154 (1998). A reassessment of relationship between riser and downcomer gas holdups in airlift reactors.
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    • Chisti, Y. and M. Moo-Young, Trans. I. Chem. Eng., 71C, 209214 (1993). Airlift bioreactors with packed beds of immobilized biocatalysts: Theoretical evaluation of the liquid circulation performance.
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    • Animal cell culture in stirred bioreactors: Observations on scale up.
    • Chisti, Y., Bioprocess. Eng., 9, 191-196 (1993) Animal cell culture in stirred bioreactors: Observations on scale up.
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    • Chisti, Y., Process Biochem., 28, 511-517 (1993). Animal cell culture in stirred bioreactors: Observations on scale up.
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    • Solid substrate fermentations, enzyme production, and food enrichment
    • Flickinger, M.C. and S.W. Drew, eds., Wiley, New York
    • Chisti, Y., Solid substrate fermentations, enzyme production, and food enrichment, in Encyclopedia of Bioprocess Technology: Fermentation, Biocatalysis, and Bioseparation, Vol. 5, Flickinger, M.C. and S.W. Drew, eds., Wiley, New York, 1999, pp. 2446-2462.
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    • Comparative evaluation of compact photobioreactors for largescale monoculture of microalgae.
    • Mirón, A.S., A.C. Gómez, F.G. Camacho, E.M. Grima, and Y. Chisti, J. Biotechnol., 70, 249-270 (1999). Comparative evaluation of compact photobioreactors for largescale monoculture of microalgae.
    • (1999) J. Biotechnol , vol.70 , pp. 249-270
    • Mirón, A.S.1    Gómez, A.C.2    Camacho, F.G.3    Grima, E.M.4    Chisti, Y.5
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    • Photobioreactors: light regime, mass transfer, and scale up.
    • Grima, E.M., F.G.A. Fernández, F.G. Camacho, and Y. Chisti, J. Biotechnol., 70, 231-247 (1999). Photobioreactors: light regime, mass transfer, and scale up.
    • (1999) J. Biotechnol , vol.70 , pp. 231-247
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    • Airlift-driven external-loop tubular photobioreactors for outdoor production of microalgae: Assessment of design and performance.
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    • (2001) Chem. Eng. Sci , vol.56 , pp. 2721-2732
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    • Tissue-type plasminogen activator: Characteristics, applications, and production technology.
    • Rouf, S.A., M. Moo-Young, and Y. Chisti, Biotechnol. Adv., 14, 239-266 (1996). Tissue-type plasminogen activator: Characteristics, applications, and production technology.
    • (1996) Biotechnol. Adv , vol.14 , pp. 239-266
    • Rouf, S.A.1    Moo-Young, M.2    Chisti, Y.3
  • 284
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    • Disruption of a recombinant yeast for the release of beta-galactosidase.
    • Garrido, F., U.C. Banerjee, Y. Chisti, and M. Moo-Young, Bioseparation, 4, 319-328 (1994). Disruption of a recombinant yeast for the release of beta-galactosidase.
    • (1994) Bioseparation , vol.4 , pp. 319-328
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    • Isolation of a recombinant intracellular beta-galactosidase by ammonium sulfate fractionation of cell homogenates.
    • Zhang, Z., Y. Chisti, and M. Moo-Young, Bioseparation, 5, 329-337 (1995). Isolation of a recombinant intracellular beta-galactosidase by ammonium sulfate fractionation of cell homogenates.
    • (1995) Bioseparation , vol.5 , pp. 329-337
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    • (1999) Encyclopedia of Bioprocess Technology: Fermentation, Biocatalysis, and Bioseparation , vol.5 , pp. 2446-2462
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    • Tamer, I. M. and Y. Chisti, Enzyme Microb. Technology, 29, 611-620 (2001). Production and recovery of recombinant protease inhibitor alpha-1-antitrypsin.
    • (2001) Enzyme Microb. Technology , vol.29 , pp. 611-620
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    • Production, purification, characterization, and applications of lipases.
    • Sharma, R., Y. Chisti, and U.C. Banerjee, Biotechnol. Adv., 19, 627-662 (2001). Production, purification, characterization, and applications of lipases.
    • (2001) Biotechnol. Adv , vol.19 , pp. 627-662
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    • Considerations for designing bioreactors for shear-sensitive culture.
    • Moo-Young, M. and Y. Chisti, Biotechnology, 6(11), 1291-1296 (1988). Considerations for designing bioreactors for shear-sensitive culture.
    • (1988) Biotechnology , vol.6 , Issue.11 , pp. 1291-1296
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    • On the calculation of shear rate and apparent viscosity in airlift and bubble column bioreactors.
    • Chisti, Y. and M. Moo-Young, Biotechnol. Bioeng., 34, 1391-1392 (1989). On the calculation of shear rate and apparent viscosity in airlift and bubble column bioreactors.
    • (1989) Biotechnol. Bioeng , vol.34 , pp. 1391-1392
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    • Effects of the hydrodynamic environment and shear protectants on survival of erythrocytes in suspension.
    • Zhang, Z., Y. Chisti, and M. Moo-Young, J. Biotechnol., 43, 33-40 (1995). Effects of the hydrodynamic environment and shear protectants on survival of erythrocytes in suspension.
    • (1995) J. Biotechnol , vol.43 , pp. 33-40
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    • Hydrodynamic damage to animal cells.
    • Chisti, Y., Crit. Rev. Biotechnol., 21, 67-110 (2001). Hydrodynamic damage to animal cells.
    • (2001) Crit. Rev. Biotechnol , vol.21 , pp. 67-110
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    • Animal cell damage in sparged bioreactors.
    • Chisti, Y., Trends Biotechnol., 18, 420-432 (2000). Animal cell damage in sparged bioreactors.
    • (2000) Trends Biotechnol , vol.18 , pp. 420-432
    • Chisti, Y.1


* 이 정보는 Elsevier사의 SCOPUS DB에서 KISTI가 분석하여 추출한 것입니다.