1969
DOI: 10.1061/jsedai.0000952
|View full text |Cite
|
Sign up to set email alerts
|

Design Principles of Waste Stabilization Ponds

Help me understand this report

Search citation statements

Order By: Relevance

Paper Sections

Select...
2
1
1
1

Citation Types

0
5
0
4

Year Published

1980
1980
2024
2024

Publication Types

Select...
4
2
2

Relationship

0
8

Authors

Journals

citations
Cited by 36 publications
(9 citation statements)
references
References 0 publications
0
5
0
4
Order By: Relevance
“…L f is adjusted based on the phenomenon found in Muttamara and Puetpaiboon [22], that is, an increase in baffle number would lead to an increase in total biofilm biomass but a decrease in biofilm thickness. θ is the temperature coefficient, with Mara [32] and Thirumurthi [33] calculating the value of θ as 1.05 and 1.036, respectively, and this is used for adjusting k fa and k fs . All equations are summarized in the Supplementary Material in Table S1.…”
Section: Application Of First-order Kinetics To Determine the Contrib...mentioning
confidence: 99%
“…L f is adjusted based on the phenomenon found in Muttamara and Puetpaiboon [22], that is, an increase in baffle number would lead to an increase in total biofilm biomass but a decrease in biofilm thickness. θ is the temperature coefficient, with Mara [32] and Thirumurthi [33] calculating the value of θ as 1.05 and 1.036, respectively, and this is used for adjusting k fa and k fs . All equations are summarized in the Supplementary Material in Table S1.…”
Section: Application Of First-order Kinetics To Determine the Contrib...mentioning
confidence: 99%
“…Marais and Shaw created a Pond equation that included first-order kinetics reaction with completely mixed circumstances (Spellman & Drinan, 2014). Designers may also utilize this equation for aerobic pond design: Epa, 2011;Thirumurthi, 1974). Where C n is the effluent BOD 5 concentration in mille grams per liter; Co is the incoming BOD 5 concentration in mille grams per liter; k c is the first-order reaction rate of the complete mixture flow, t n is the hydraulic residence time in each cell, in days; and n is the number of pond cells of the same size.…”
Section: Design Of Oxidation Ponds As Chemical Reactormentioning
confidence: 99%
“…Where C n is the effluent BOD 5 concentration in mille grams per liter; Co is the incoming BOD 5 concentration in mille grams per liter; k c is the first-order reaction rate of the complete mixture flow, t n is the hydraulic residence time in each cell, in days; and n is the number of pond cells of the same size. The application of Thirumurthi contended that Marais and Shaw's assumption of fully mixed circumstances was not optimal for aerated pond design, but chemical reaction proposals were perfect (Zimmo et al, 2003;Thirumurthi, 1974).…”
Section: Design Of Oxidation Ponds As Chemical Reactormentioning
confidence: 99%
“…The hydraulic regime in facultative ponds, and in all waste stabilization ponds, is dispersed flow (Thirumurthi, 1969). The most efficient hydraulic regime is plug flow, in which designs should always attempt to approximate by minimizing as much as possible the effects of dispersion.…”
Section: Longitudinal Dispersionmentioning
confidence: 99%
“…The model of dispersion is used for E. coli or fecal coliform reduction in both facultative and maturation ponds. The Wehner and Wilhem equation (Wehner & Wilhelm, 1956), which was recommended by Thirumurthi (1969) for the design of facultative ponds, is used in the following form:…”
Section: E Coli or Fecal Coliform Reductionmentioning
confidence: 99%