Gas-lift anaerobic dynamic membrane bioreactors for high strength synthetic wastewater treatment: Effect of biogas sparging velocity and HRT on treatment performance

Mustafa Evren Ersahin; Juan B. Gimenez; Hale Ozgun; Yu Tao; Henri Spanjers; Jules B. van Lier

doi:10.1016/j.cej.2016.02.003

Gas-lift anaerobic dynamic membrane bioreactors for high strength synthetic wastewater treatment: Effect of biogas sparging velocity and HRT on treatment performance

Mustafa Evren Ersahin^*
, Juan B. Gimenez
, Hale Ozgun
, Yu Tao
, Henri Spanjers
, Jules B. van Lier

^*Bu çalışma için yazışmadan sorumlu yazar

Çevre Mühendisliği Bölümü

Delft University of Technology
University of Valencia
Harbin Institute of Technology

Araştırma sonucu: Dergiye katkı › Makale › bilirkişi

59 Atıf (Scopus)

Özet

A laboratory scale external anaerobic dynamic membrane bioreactor (AnDMBR) treating high strength wastewater (influent COD ≈ 20 g/L) was operated to assess the effect of biogas sparging velocity (GSV) and hydraulic retention time (HRT) on removal efficiency and dynamic membrane (DM) filtration characteristics. An increase in GSV resulted in a decrease in DM filtration resistance. DM or cake layer was identified as the main contributor to the total filtration resistance. The external AnDMBR achieved over 99% COD removal efficiency irrespective of the GSV. The results showed that the DM formation process proceeded until a stable cake layer was reached. Reducing of HRT resulted in an increase in protein/carbohydrate ratio in soluble microbial products (SMP) and an increase in biomass concentration in the bioreactor. Therefore, HRT affected TMP and total filtration resistance in the AnDMBR. A high permeate quality was obtained by an effective DM layer at organic loading rates (OLRs) between 2 and 3.6 kg COD/m³ d. Based on the fluxes observed in this research, the filter cloth costs would be in the range of 0.17 €/m³ of treated wastewater. The investment and operational costs of the AnDMBRs are expected to be substantially lower than that of conventional membrane filtration.

Orijinal dil	İngilizce
Sayfa (başlangıç-bitiş)	46-53
Sayfa sayısı	8
Dergi	Chemical Engineering Journal
Hacim	305
DOI'lar	https://doi.org/10.1016/j.cej.2016.02.003
Yayın durumu	Yayınlandı - 1 Ara 2016

Bibliyografik not

Publisher Copyright:
© 2016 Elsevier B.V.

Finansman

The authors would like to express their gratitude for the PhD Fellowship awards provided by HUYGENS Scholarship Programme to M. Evren Ersahin, by the Spanish Ministry of Economy and Competitiveness to Juan B. Gimenez, by the Turkish Academy of Sciences (TUBA) to Hale Ozgun and by the China Scholarship Council to Yu Tao. This publication was produced as part of the DynaFil project in which KWR Watercycle Research Institute, TU Delft, Waternet, STOWA, Logisticon Water Treatment, Waterboard Brabantse Delta and Bert Daamen participate. The project (EVTP01084) is partly funded by the Dutch Government via AgentschapNL under the Energy and Innovation Grant, Effective and Efficient Digestion chain.

Finansörler	Finansör numarası
AgentschapNL
Dutch Government
TUBA
Ministerio de Economía y Competitividad
Türkiye Bilimler Akademisi
China Scholarship Council	EVTP01084

BM SKH

Bu sonuç, aşağıdaki Sürdürülebilir Kalkınma Hedefine/Hedeflerine katkıda bulunur

SKH 6 Temiz Su ve Sanitasyon

Belgeye Erişim

10.1016/j.cej.2016.02.003

Diğer Dosyalar ve Linkler

Link to publication in Scopus

Alıntı Yap

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title = "Gas-lift anaerobic dynamic membrane bioreactors for high strength synthetic wastewater treatment: Effect of biogas sparging velocity and HRT on treatment performance",

abstract = "A laboratory scale external anaerobic dynamic membrane bioreactor (AnDMBR) treating high strength wastewater (influent COD ≈ 20 g/L) was operated to assess the effect of biogas sparging velocity (GSV) and hydraulic retention time (HRT) on removal efficiency and dynamic membrane (DM) filtration characteristics. An increase in GSV resulted in a decrease in DM filtration resistance. DM or cake layer was identified as the main contributor to the total filtration resistance. The external AnDMBR achieved over 99\% COD removal efficiency irrespective of the GSV. The results showed that the DM formation process proceeded until a stable cake layer was reached. Reducing of HRT resulted in an increase in protein/carbohydrate ratio in soluble microbial products (SMP) and an increase in biomass concentration in the bioreactor. Therefore, HRT affected TMP and total filtration resistance in the AnDMBR. A high permeate quality was obtained by an effective DM layer at organic loading rates (OLRs) between 2 and 3.6 kg COD/m3 d. Based on the fluxes observed in this research, the filter cloth costs would be in the range of 0.17 €/m3 of treated wastewater. The investment and operational costs of the AnDMBRs are expected to be substantially lower than that of conventional membrane filtration.",

keywords = "Anaerobic membrane bioreactor, Dynamic membrane, Feasibility, Gas sparging velocity, Wastewater treatment",

author = "Ersahin, \{Mustafa Evren\} and Gimenez, \{Juan B.\} and Hale Ozgun and Yu Tao and Henri Spanjers and \{van Lier\}, \{Jules B.\}",

note = "Publisher Copyright: {\textcopyright} 2016 Elsevier B.V.",

year = "2016",

month = dec,

day = "1",

doi = "10.1016/j.cej.2016.02.003",

language = "English",

volume = "305",

pages = "46--53",

journal = "Chemical Engineering Journal",

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publisher = "Elsevier B.V.",

}

TY - JOUR

T1 - Gas-lift anaerobic dynamic membrane bioreactors for high strength synthetic wastewater treatment

T2 - Effect of biogas sparging velocity and HRT on treatment performance

AU - Ersahin, Mustafa Evren

AU - Gimenez, Juan B.

AU - Ozgun, Hale

AU - Tao, Yu

AU - Spanjers, Henri

AU - van Lier, Jules B.

PY - 2016/12/1

Y1 - 2016/12/1

N2 - A laboratory scale external anaerobic dynamic membrane bioreactor (AnDMBR) treating high strength wastewater (influent COD ≈ 20 g/L) was operated to assess the effect of biogas sparging velocity (GSV) and hydraulic retention time (HRT) on removal efficiency and dynamic membrane (DM) filtration characteristics. An increase in GSV resulted in a decrease in DM filtration resistance. DM or cake layer was identified as the main contributor to the total filtration resistance. The external AnDMBR achieved over 99% COD removal efficiency irrespective of the GSV. The results showed that the DM formation process proceeded until a stable cake layer was reached. Reducing of HRT resulted in an increase in protein/carbohydrate ratio in soluble microbial products (SMP) and an increase in biomass concentration in the bioreactor. Therefore, HRT affected TMP and total filtration resistance in the AnDMBR. A high permeate quality was obtained by an effective DM layer at organic loading rates (OLRs) between 2 and 3.6 kg COD/m3 d. Based on the fluxes observed in this research, the filter cloth costs would be in the range of 0.17 €/m3 of treated wastewater. The investment and operational costs of the AnDMBRs are expected to be substantially lower than that of conventional membrane filtration.

AB - A laboratory scale external anaerobic dynamic membrane bioreactor (AnDMBR) treating high strength wastewater (influent COD ≈ 20 g/L) was operated to assess the effect of biogas sparging velocity (GSV) and hydraulic retention time (HRT) on removal efficiency and dynamic membrane (DM) filtration characteristics. An increase in GSV resulted in a decrease in DM filtration resistance. DM or cake layer was identified as the main contributor to the total filtration resistance. The external AnDMBR achieved over 99% COD removal efficiency irrespective of the GSV. The results showed that the DM formation process proceeded until a stable cake layer was reached. Reducing of HRT resulted in an increase in protein/carbohydrate ratio in soluble microbial products (SMP) and an increase in biomass concentration in the bioreactor. Therefore, HRT affected TMP and total filtration resistance in the AnDMBR. A high permeate quality was obtained by an effective DM layer at organic loading rates (OLRs) between 2 and 3.6 kg COD/m3 d. Based on the fluxes observed in this research, the filter cloth costs would be in the range of 0.17 €/m3 of treated wastewater. The investment and operational costs of the AnDMBRs are expected to be substantially lower than that of conventional membrane filtration.

KW - Anaerobic membrane bioreactor

KW - Dynamic membrane

KW - Feasibility

KW - Gas sparging velocity

KW - Wastewater treatment

UR - https://www.scopus.com/pages/publications/84991075535

U2 - 10.1016/j.cej.2016.02.003

DO - 10.1016/j.cej.2016.02.003

M3 - Article

AN - SCOPUS:84991075535

SN - 1385-8947

VL - 305

SP - 46

EP - 53

JO - Chemical Engineering Journal

JF - Chemical Engineering Journal

ER -

Gas-lift anaerobic dynamic membrane bioreactors for high strength synthetic wastewater treatment: Effect of biogas sparging velocity and HRT on treatment performance

Özet

Bibliyografik not

Finansman

BM SKH

Belgeye Erişim

Diğer Dosyalar ve Linkler

Parmak izi

Alıntı Yap