A kinetic study of a membrane anaerobic reactor (MAR) for treatment of sewage sludge

被引：35

作者：

Abdullah, AGL ^{[1
]}

Idris, A ^{[1
]}

Ahmadun, FR ^{[1
]}

Baharin, BS ^{[1
]}

Emby, F ^{[1
]}

Noor, MJMM ^{[1
]}

Nour, AH ^{[1
]}

机构：

[1] Univ Putra Malaysia, Serdang 43400, Selangor, Malaysia

来源：

DESALINATION | 2005年 / 183卷 / 1-3期

关键词：

kinetics; sewage sludge; anaerobic; membrane; ultrafiltration; WASTE-WATER TREATMENT; ADUF PROCESS; SEPARATION; EFFLUENT; SCALE;

D O I：

10.1016/j.desal.2005.03.044

中图分类号：

TQ [化学工业];

学科分类号：

0817 ;

摘要：

The application of kinetic models (Monod, Contois and Chen & Hashimoto) and overall microbial kinetic on the membrane anaerobic reactor (MAR) for treatment of sewage sludge was investigated. The system consists of a cross-flow ultrafiltration membrane and six steady states were attained over a range of mixed liquor suspended solids of 12,760-21,800 mg/l. The results of all six steady states were successfully fitted above 98% for three known kinetics. The growth yield coefficient, Y, was found to be 0.74 gVSS/gCOD while the specific microorganism decay rate was 0.20 d(-1). The k values were in the range of 0.350-0.519 gCOD/gVSS.d and mu(max) values were between 0.259 and 0.384 d(-1). The COD removal efficiency was 96.5-99% with HRT of 7.8 days. The methane gas yield was between 0.19 l/g COD/d to 0.54 l/g COD/d when the organic loading rate increased from 0.1 kg COD/m(3)/d to 10 kg COD/m(3)/d. The system efficiency was greatly influenced by SRT and OLRs. Membrane flux rate deterioration was observed from 62.1 l/m(2)/h to 6.9 l/m(2)/h due to membrane fouling.

引用

页码：439 / 445

页数：7

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