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Solid effluent flux can be calculated directly from this model.
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Effluent mass flux values were normalized by the up-gradient DNAPL distributions.
Effluent mass flux due to water dissolution was also found to increase progressively due to the increase in NAPL-water contact area even though the PCE mass was reduced.
In view of all such constraints and limitations, a biofilm model is thus developed with a computer programming in FORTRAN to easily calculate the output parameters like effluent substrate concentration, substrate flux as well as effective and total biofilm thickness.
At an operating pressure of 1 kg/cm2, the flux value of effluent 1 was about 9 to 15 LMH, whereas for effluent 2 it was about 17.9 to 21 LMH and for effluent 3 it was about 23.5 to 27.5 LMH.
Leaf infusions obtained by infusing plant leaves with water at room temperature were introduced into a wet effluent denuder fed with a flux of ozone-rich air.
The average flux value for effluents 1, 2 and 3 was about 13, 19 and 24 LMH2/h (LMH), respectively.
Open image in new window Figure 5 Flux vs time (a) and variation of flux (b) with transmembrane pressure for tannery effluent on different days.
Water flux and chemical composition of effluent waters were monitored during almost 4 years.
Water flux and chemical data of effluent waters were measured during the experiment.
The model solutions included the concentration profiles of inorganic carbon in the microalgal biofilm, the growths of suspended microalgae and microalgal biofilm, the effluent concentrations of inorganic carbon, and the flux of inorganic carbon from bulk liquid into biofilm.
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