Diffusion controlled transient kinetics of the reaction of carbon monoxide with myoglobin in a supercooled very high viscosity glycerol-water solvent

1978 ◽  
Vol 82 (24) ◽  
pp. 2630-2631 ◽  
Author(s):  
Brian B. Hasinoff
Keyword(s):  
Carbon Monoxide ◽  
High Viscosity ◽  
Transient Kinetics ◽  
Glycerol Water ◽  
Water Solvent ◽  
Diffusion Controlled ◽  
Kinetics Of ◽  
Very High

Simultaneous diffusion and chemical activation control of the kinetics of the binding of carbon monoxide to ferroprotoporphyrin IX in glycerol–water mixtures of high viscosity

1977 ◽  
Vol 55 (23) ◽  
pp. 3955-3960 ◽  
Author(s):  
Brian B. Hasinoff
Keyword(s):  
Diffusion Rate ◽  
Chemical Activation ◽  
High Viscosity ◽  
Diffusion Control ◽  
Glycerol Water ◽  
Diffusion Controlled ◽  
Kinetics Of ◽  
And Diffusion ◽  
Simultaneous Influence ◽  
Diffusion Controlled Reaction

The kinetics of the reaction of ferroprotoporphyrin IX with CO have been studied in mixed glycerol–water solvents of high viscosity in order that the simultaneous influence of chemical activation and diffusion control of the reaction might be observed. Analyses of curved Arrhenius plots indicated that in the low temperature high viscosity limits the reaction is largely diffusion controlled. The deviation of the second order diffusion rate constants, from that predicted by simple theory for reaction between uniformly reactive spheres of equal radii, is a factor of 0.3 to 0.9, depending upon the solvent composition. A couple of other models for diffusion controlled reaction, ascribing these deviations to changes of steric requirements, were also examined.

The effect of heterotrophic yield on the assessment of the correction factor for anoxic growth

1996 ◽  
Vol 34 (5-6) ◽  
pp. 67-74 ◽  
Author(s):  
D. Orhon ◽  
S. Sözen ◽  
N. Artan
Keyword(s):  
Correction Factor ◽  
Domestic Sewage ◽  
Yield Coefficient ◽  
Heterotrophic Growth ◽  
Metabolic Processes ◽  
Anoxic Conditions ◽  
Industrial Wastewaters ◽  
Systems Modelling ◽  
Kinetics Of ◽  
Very High

For single-sludge denitrification systems, modelling of anoxic reactors currently uses the kinetics of aerobic heterotrophic growth together with a correction factor for anoxic conditions. This coefficient is computed on the basis of respirometric measurements with the assumption that the heterotrophic yield remains the same under aerobic and anoxic coditions. The paper provides the conceptual proof that the yield coefficient is significantly lower for the anoxic growth on the basis of the energetics of the related metabolic processes. This is used for the interpretation of the very high values for the correction factor experimentally determined for a number of industrial wastewaters. A default value for the anoxic heterotrophic yield coefficient is calculated for domestic sewage and compatible wastewaters and proposed for similar evaluations.

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