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Steady-state analysis of activated sludge processes with a settler model including sludge compression

Diehl, Stefan (author)
Lund University,Lunds universitet,Partiella differentialekvationer,Forskargrupper vid Lunds universitet,Matematik LTH,Matematikcentrum,Institutioner vid LTH,Lunds Tekniska Högskola,Partial differential equations,Lund University Research Groups,Mathematics (Faculty of Engineering),Centre for Mathematical Sciences,Departments at LTH,Faculty of Engineering, LTH
Zambrano, Jesús (author)
Uppsala universitet,Avdelningen för systemteknik,Reglerteknik
Carlsson, Bengt (author)
Uppsala universitet,Avdelningen för systemteknik,Reglerteknik
 (creator_code:org_t)
Elsevier BV, 2016
2016
English.
In: Water Research. - : Elsevier BV. - 1879-2448 .- 0043-1354. ; 88:1, s. 104-116
  • Journal article (peer-reviewed)
Abstract Subject headings
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  • A reduced model of a completely stirred-tank bioreactor coupled to a settling tank with recycle is analyzed in its steady states. In the reactor, the concentrations of one dominant particulate biomass and one soluble substrate component are modelled. While the biomass decay rate is assumed to be constant, growth kinetics can depend on both substrate and biomass concentrations, and optionally model substrate inhibition. Compressive and hindered settling phenomena are included using the Bürger-Diehl settler model, which consists of a partial differential equation. Steady-state solutions of this partial differential equation are obtained from an ordinary differential equation, making steady-state analysis of the entire plant difficult. A key result showing that the ordinary differential equation can be replaced with an approximate algebraic equation simplifies model analysis. This algebraic equation takes the location of the sludge-blanket during normal operation into account, allowing for the limiting flux capacity caused by compressive settling to easily be included in the steady-state mass balance equations for the entire plant system. This novel approach grants the possibility of more realistic solutions than other previously published reduced models, comprised of yet simpler settler assumptions. The steady-state concentrations, solids residence time, and the wastage flow ratio are functions of the recycle ratio. Solutions are shown for various growth kinetics; with different values of biomass decay rate, influent volumetric flow, and substrate concentration.

Subject headings

NATURVETENSKAP  -- Matematik (hsv//swe)
NATURAL SCIENCES  -- Mathematics (hsv//eng)
TEKNIK OCH TEKNOLOGIER  -- Kemiteknik (hsv//swe)
ENGINEERING AND TECHNOLOGY  -- Chemical Engineering (hsv//eng)
TEKNIK OCH TEKNOLOGIER  -- Miljöbioteknik -- Vattenbehandling (hsv//swe)
ENGINEERING AND TECHNOLOGY  -- Environmental Biotechnology -- Water Treatment (hsv//eng)
TEKNIK OCH TEKNOLOGIER  -- Samhällsbyggnadsteknik -- Vattenteknik (hsv//swe)
ENGINEERING AND TECHNOLOGY  -- Civil Engineering -- Water Engineering (hsv//eng)
TEKNIK OCH TEKNOLOGIER  -- Elektroteknik och elektronik -- Reglerteknik (hsv//swe)
ENGINEERING AND TECHNOLOGY  -- Electrical Engineering, Electronic Engineering, Information Engineering -- Control Engineering (hsv//eng)

Keyword

Bioreactor
Bürger-Diehl settler model
Growth kinetics
Limiting flux
Secondary settling tank
Solids residence time (SRT).
Bioreactor; Burger-Diehl settler model; Growth kinetics; Limiting flux; Secondary settling tank; Solids residence time (SAT)

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art (subject category)
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Diehl, Stefan
Zambrano, Jesús
Carlsson, Bengt
About the subject
NATURAL SCIENCES
NATURAL SCIENCES
and Mathematics
ENGINEERING AND TECHNOLOGY
ENGINEERING AND ...
and Chemical Enginee ...
ENGINEERING AND TECHNOLOGY
ENGINEERING AND ...
and Environmental Bi ...
and Water Treatment
ENGINEERING AND TECHNOLOGY
ENGINEERING AND ...
and Civil Engineerin ...
and Water Engineerin ...
ENGINEERING AND TECHNOLOGY
ENGINEERING AND ...
and Electrical Engin ...
and Control Engineer ...
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Water Research
By the university
Lund University
Uppsala University

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