1983
DOI: 10.1002/bit.260251002
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Rates of glucose oxidation with a column reactor utilizing a magnetic field

Abstract: Rates of glucose oxidation were measured with the use of a fluidized-bed column placed in a magnetic field and magnetite-containing beads of immobilized glucose oxidase and catalase. Its performance was predicted from the volumetric coefficient for liquid-phase mass transfer and the kinetic constants for glucose oxidation. Effusion of beads was negligible under the operating conditions employed.

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Cited by 20 publications
(4 citation statements)
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“…To some extent, compounds based on Ca-alginate (Sajc et al 1995(Sajc et al ,1996 doped with magnetite and magnetic cores covered by nonmagnetic layers such as activated carbon and zeolite (Penchev et al, 1991;Al-Qodah, 2002a) are employed. In some studies (on bubble dynamics and gas holdup) surfactants similar to those in classical hydrodynamics experiments with bubble columns (Fan, 1989) Sada et al, (1983) -field distribution c) Wu (1987, 1988)-hydrodynamic experiments. Short coils based system.…”
Section: Solids Liquids and Gasesmentioning
confidence: 98%
See 1 more Smart Citation
“…To some extent, compounds based on Ca-alginate (Sajc et al 1995(Sajc et al ,1996 doped with magnetite and magnetic cores covered by nonmagnetic layers such as activated carbon and zeolite (Penchev et al, 1991;Al-Qodah, 2002a) are employed. In some studies (on bubble dynamics and gas holdup) surfactants similar to those in classical hydrodynamics experiments with bubble columns (Fan, 1989) Sada et al, (1983) -field distribution c) Wu (1987, 1988)-hydrodynamic experiments. Short coils based system.…”
Section: Solids Liquids and Gasesmentioning
confidence: 98%
“…Magnetically assisted airlifts Onto tehi Fig. 3 Examples of gas-liquid distributor designs used in magnetically threephase fluidization Schematically a) Sada(1983) b) Sada(1983) c) Penchevetal. (1991) d) HuandWu (1987) -hydrodynamic experiments e) HuandWu (1987) phenol degradation f) Hristov (1998aHristov ( ,2005a …”
Section: Fluidization Units -Columns and Distributor Designsmentioning
confidence: 99%
“…Among these new contactors, fluidized beds and packed beds are being considered as promising reactors suitable for carrying out bioprocesses with immobilized biocatalysts [1,2]. Subsequently, magnetically stabilized fluidized beds (MSFBs) have been applied to conduct bioprocesses with immobilized biocatalyst on magnetic particles as a solid phase, thereby presenting further options in continuous reactor systems [3][4][5]. This technology is expected to show potential applications in various areas such as bioseparations and immobilized biocatalyst systems [6][7][8][9][10][11][12].…”
Section: Introductionmentioning
confidence: 99%
“…Currently fluidized beds are used as three-phase reactors (Sada, 1983;Musgrave, 1982). However, vigorous bubbling to improve gas absorption rate requires excessive aeration energy and will damage beads with immobilzed enzymes.…”
Section: Introductionmentioning
confidence: 99%