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222 related items for PubMed ID: 15748765

  • 1. Gas holdup, foaming and oxygen transfer in a jet loop bioreactor with artificial foaming media and yeast culture.
    Flores-Cotera LB, García-Salas S.
    J Biotechnol; 2005 Apr 06; 116(4):387-96. PubMed ID: 15748765
    [Abstract] [Full Text] [Related]

  • 2. Computational-fluid-dynamics (CFD) analysis of mixing and gas-liquid mass transfer in shake flasks.
    Zhang H, Williams-Dalson W, Keshavarz-Moore E, Shamlou PA.
    Biotechnol Appl Biochem; 2005 Feb 06; 41(Pt 1):1-8. PubMed ID: 15310285
    [Abstract] [Full Text] [Related]

  • 3. Characteristics of three-phase internal loop airlift bioreactors with complete gas recirculation for non-Newtonian fluids.
    Wen J, Jia X, Cheng X, Yang P.
    Bioprocess Biosyst Eng; 2005 May 06; 27(3):193-205. PubMed ID: 15765215
    [Abstract] [Full Text] [Related]

  • 4. Enhancement of oxygen mass transfer in stirred bioreactors using oxygen-vectors. 1. Simulated fermentation broths.
    Galaction AI, Cascaval D, Oniscu C, Turnea M.
    Bioprocess Biosyst Eng; 2004 Jul 06; 26(4):231-8. PubMed ID: 15042455
    [Abstract] [Full Text] [Related]

  • 5. Gas holdup and overall volumetric oxygen transfer coefficient in airlift contactors.
    Bello RA, Robinson CW, Moo-Young M.
    Biotechnol Bioeng; 1985 Mar 06; 27(3):369-81. PubMed ID: 18553682
    [Abstract] [Full Text] [Related]

  • 6. Submerged monoxenic culture of the entomopathogenic nematode Steinernema carpocapsae in an internal-loop airlift bioreactor using two configurations of the inner tube.
    Chavarría-Hernández N, Sanjuan-Galindo R, Rodríguez-Pastrana BR, Medina-Torres L, Rodríguez-Hernández AI.
    Biotechnol Bioeng; 2007 Sep 01; 98(1):167-76. PubMed ID: 17252612
    [Abstract] [Full Text] [Related]

  • 7. Effect of sparger design on hydrodynamics of a gas recirculation anaerobic bioreactor.
    Varma R, Al-Dahhan M.
    Biotechnol Bioeng; 2007 Dec 15; 98(6):1146-60. PubMed ID: 17514754
    [Abstract] [Full Text] [Related]

  • 8. Characterization of a pilot plant airlift tower loop bioreactor. I: evaluation of the phase properties with model media.
    Fröhlich S, Lotz M, Korte T, Lübbert A, Schügerl K, Seekamp M.
    Biotechnol Bioeng; 1991 Jun 05; 38(1):43-55. PubMed ID: 18600697
    [Abstract] [Full Text] [Related]

  • 9. Characterization of gas-liquid mass transfer phenomena in microtiter plates.
    Hermann R, Lehmann M, Büchs J.
    Biotechnol Bioeng; 2003 Jan 20; 81(2):178-86. PubMed ID: 12451554
    [Abstract] [Full Text] [Related]

  • 10. Prediction of gas-liquid mass transfer coefficient in sparged stirred tank bioreactors.
    Garcia-Ochoa F, Gomez E.
    Biotechnol Bioeng; 2005 Dec 20; 92(6):761-72. PubMed ID: 16155951
    [Abstract] [Full Text] [Related]

  • 11. Characterization of a pilot plant airlift tower loop reactor: III. Evaluation of local properties of the dispersed gas phase during yeast cultivation and in model media.
    Fröhlich S, Lotz M, Larson B, Lübbert A, Schügerl K, Seekamp M.
    Biotechnol Bioeng; 1991 Jun 05; 38(1):56-64. PubMed ID: 18600698
    [Abstract] [Full Text] [Related]

  • 12. Enhancing oxygen transfer in surface-aerated bioreactors by stable foams.
    Ju LK, Armiger WB.
    Biotechnol Prog; 1990 Jun 05; 6(4):262-5. PubMed ID: 1366762
    [Abstract] [Full Text] [Related]

  • 13. Hydrodynamics and mass transfer in Aspergillus niger fermentations in bubble column and loop bioreactors.
    Allen DG, Robinson CW.
    Biotechnol Bioeng; 1989 Sep 05; 34(6):731-40. PubMed ID: 18588159
    [Abstract] [Full Text] [Related]

  • 14. Microbial biomass production from rice straw hydrolysate in airlift bioreactors.
    Zheng YG, Chen XL, Wang Z.
    J Biotechnol; 2005 Sep 10; 118(4):413-20. PubMed ID: 15978690
    [Abstract] [Full Text] [Related]

  • 15. Influence of operating variables on liquid circulation in a 10.5-m(3) jet loop bioreactor.
    García-Salas S, Flores-Cotera LB.
    Biotechnol Bioeng; 1995 Jun 05; 46(5):408-14. PubMed ID: 18623331
    [Abstract] [Full Text] [Related]

  • 16. [Physiological aspects of intensifying yeast growth].
    Shkidchenko AN.
    Prikl Biokhim Mikrobiol; 2006 Jun 05; 42(2):213-8. PubMed ID: 16761577
    [Abstract] [Full Text] [Related]

  • 17. Oxygen transfer and gas holdup in airlift bioreactors assembled with helical flow promoters.
    Picão BW, Gonçalves DO, Ribeiro RMMGP, Esperança MN, Peixoto G, Cerri MO.
    Bioprocess Biosyst Eng; 2023 May 05; 46(5):681-692. PubMed ID: 36806976
    [Abstract] [Full Text] [Related]

  • 18. Development, parallelization, and automation of a gas-inducing milliliter-scale bioreactor for high-throughput bioprocess design (HTBD).
    Puskeiler R, Kaufmann K, Weuster-Botz D.
    Biotechnol Bioeng; 2005 Mar 05; 89(5):512-23. PubMed ID: 15669089
    [Abstract] [Full Text] [Related]

  • 19. Simplified soy molasses-based medium for reduced-cost production of sophorolipids by Candida bombicola.
    Solaiman DK, Ashby RD, Zerkowski JA, Foglia TA.
    Biotechnol Lett; 2007 Sep 05; 29(9):1341-7. PubMed ID: 17541506
    [Abstract] [Full Text] [Related]

  • 20. Improvement of foam breaking and oxygen-transfer performance in a stirred-tank fermenter.
    Takesono S, Onodera M, Toda K, Yoshida M, Yamagiwa K, Ohkawa A.
    Bioprocess Biosyst Eng; 2006 Mar 05; 28(4):235-42. PubMed ID: 16208498
    [Abstract] [Full Text] [Related]

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