Model assisted startup of anaerobic digesters fed with thermally hydrolysed activated sludge

被引:21
作者
Batstone, D. J. [1 ]
Balthes, C. [2 ]
Barr, K. [2 ]
机构
[1] Univ Queensland, Adv Wastewater Management Ctr, Brisbane, Qld 4072, Australia
[2] Brisbane City Council, Rocklea, Qld, Australia
关键词
activated sludge; ADM1; ammonia inhibition; degradability; model; thermal hydrolysis; SIMULATION; REACTORS; PLANT; ADM1;
D O I
10.2166/wst.2010.487
中图分类号
X [环境科学、安全科学];
学科分类号
083001 [环境科学];
摘要
This paper presents the use of the IWA ADM1 to predict and interpret results from two full-scale anaerobic digesters fed with thermal hyrolysate (waste activated sludge with a long upstream sludge age) from a Cambi hydrolysis process operating at 165 C and 6 bar-g The first digester was fed conventionally though intermittently, while the second was heavily diluted through a substantial component of the evaluation period (110 days) There were a number of important outcomes related to both model application, and model predictions Input and inert COD mass ratio was very important, and was considerably higher than the 1 42g g(-1) used for biomass throughout the IWA activated sludge and anaerobic digestion models Input COD VS ratio was 1 6gg(-1), and inert COD VS ratio was 1 7 g g-1 The model succeeded on a number of levels, including effective prediction of important outputs (degradability, gas flow and composition, and final solids), clarification of the substantial data scatter, prediction of recovery times during operationally poor periods, and cross-validation of the results between digester 1 and digester 2 Key failures in model performance were related to an early incorrect assumption of the COD VS ratio of 1 42 gg(-1), and intermittent high acetate levels, most likely caused by inhibition, and rapid acclimatisation to ammonia The acute free ammonia limit was found to be 0 008M NH(3)-N, while the chronic inhibition constant (K(I,NH3,ac)) was 0 007 +/- 001M NH(3)-N Overall, this is a complex system, and application of the model added significant confidence to the initial operational decisions during an aggressive startup on an atypical feed.
引用
收藏
页码:1661 / 1666
页数:6
相关论文
共 15 条
[1]
[Anonymous], 2002, WATER INTELL ONLINE, DOI DOI 10.2166/9781780403052
[2]
Evaluation, selection and initial performance of a large scale centralised biosolids facility at Oxley Creek Water Reclamation Plant, Brisbane [J].
Barr, K. G. ;
Solley, D. O. ;
Starrenburg, D. J. ;
Lewis, R. G. .
WATER SCIENCE AND TECHNOLOGY, 2008, 57 (10) :1579-1586
[3]
Estimation of Hydrolysis Parameters in Full-Scale Anerobic Digesters [J].
Batstone, D. J. ;
Tait, S. ;
Starrenburg, D. .
BIOTECHNOLOGY AND BIOENGINEERING, 2009, 102 (05) :1513-1520
[4]
BATSTONE DJ, 2006, ANAEROBIC DIGESTION
[5]
Modelling of two-stage anaerobic digestion using the IWA Anaerobic Digestion Model No. 1 (ADM1) [J].
Blumensaat, F ;
Keller, J .
WATER RESEARCH, 2005, 39 (01) :171-183
[6]
ADM1-based methodology for the characterisation of the influent sludge in anaerobic reactors [J].
Huete, E. ;
de Gracia, M. ;
Ayesa, E. ;
Garcia-Heras, J. L. .
WATER SCIENCE AND TECHNOLOGY, 2006, 54 (04) :157-166
[7]
Applications and limitations of ADM 1 in municipal wastewater solids treatment [J].
Johnson, B. R. ;
Shang, Y. .
WATER SCIENCE AND TECHNOLOGY, 2006, 54 (04) :77-82
[8]
Influence of environmental conditions on methanogenic compositions in anaerobic biogas reactors [J].
Karakashev, D ;
Batstone, DJ ;
Angelidaki, I .
APPLIED AND ENVIRONMENTAL MICROBIOLOGY, 2005, 71 (01) :331-338
[9]
An ASM/ADM model interface for dynamic plant-wide simulation [J].
Nopens, Ingmar ;
Batstone, Damien J. ;
Copp, John B. ;
Jeppsson, Ulf ;
Volcke, Eveline ;
Alex, Jens ;
Vanrolleghem, Peter A. .
WATER RESEARCH, 2009, 43 (07) :1913-1923
[10]
PANTER K, 2005, 10 YEARS EXPERIENCE