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Modified fractional-order model for biomass degradation in an up-flow anaerobic sludge blanket reactor at Zenein Wastewater Treatment Plant.
El-Seddik, Mostafa M; Galal, Mona M; Rozaik, Ehab H; Radwan, Ahmed G.
Afiliación
  • El-Seddik MM; Sanitary and Environmental Engineering, Civil Engineering Department, Institute of Aviation Engineering & Technology, PhD, Giza, 12815, Egypt. mostafaelseddek@yahoo.com.
  • Galal MM; Sanitary and Environmental Engineering, Public Works Department, Faculty of Engineering, Cairo University, PhD, Cairo, 12613, Egypt.
  • Rozaik EH; Sanitary and Environmental Engineering, Public Works Department, Faculty of Engineering, Cairo University, PhD, Cairo, 12613, Egypt.
  • Radwan AG; Engineering Mathematics Department, Faculty of Engineering, Cairo University, PhD, Cairo, 12613, Egypt.
Environ Sci Pollut Res Int ; 29(17): 25980-25986, 2022 Apr.
Article en En | MEDLINE | ID: mdl-35190992
This paper presents a modified fractional-order model (FOM) for microorganism stimulation in an up-flow anaerobic sludge blanket (UASB) reactor treating low-strength wastewater. This study aimed to examine the famine period of methanogens due to biomass accumulation in the UASB reactor over long time periods at a constant organic loading rate (OLR). This modified model can investigate the substrate biodegradation in a UASB reactor while considering substrate diffusion into biological granules during the feast and famine periods of methanogens. The Grünwald-Letnikov numerical technique was used to indicate the effect of biomass degradation on the biogas production rate and substrate biodegradation in a UASB reactor installed at Zenein Wastewater Treatment Plant (WWTP) in Giza, Egypt. Several fractional orders were applied in the dynamic model at biomass concentrations of [Formula: see text] and [Formula: see text] in the reactor bed and blanket zones, respectively. An OLR of [Formula: see text] using the calibrated kinetic parameters at [Formula: see text] was applied to comply with the experimental outcomes. The simulation results indicate that the removal efficiency of chemical oxygen demand (COD) was maintained at approximately [Formula: see text], whereas the biogas production rate declined from [Formula: see text] in the reactor bed zone due to a decline in food to microorganism (F/M) ratio from [Formula: see text] during the sludge retention time (SRT) in the UASB reactor.
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Texto completo: 1 Colección: 01-internacional Base de datos: MEDLINE Asunto principal: Aguas del Alcantarillado / Purificación del Agua Idioma: En Revista: Environ Sci Pollut Res Int Asunto de la revista: SAUDE AMBIENTAL / TOXICOLOGIA Año: 2022 Tipo del documento: Article País de afiliación: Egipto Pais de publicación: Alemania

Texto completo: 1 Colección: 01-internacional Base de datos: MEDLINE Asunto principal: Aguas del Alcantarillado / Purificación del Agua Idioma: En Revista: Environ Sci Pollut Res Int Asunto de la revista: SAUDE AMBIENTAL / TOXICOLOGIA Año: 2022 Tipo del documento: Article País de afiliación: Egipto Pais de publicación: Alemania