کد مقاله | کد نشریه | سال انتشار | مقاله انگلیسی | نسخه تمام متن |
---|---|---|---|---|
147046 | 456385 | 2014 | 7 صفحه PDF | دانلود رایگان |
• A simplified anaerobic digestion model was developed.
• The performance of the reactor at lab-scale and pilot-scale was predicted.
• The influence of mixing was investigated.
• Unmixed conditions resulted at pilot-scale in reduced biogas production and VFA accumulation.
In this study it is demonstrated that a correct description of the mixing behavior of an anaerobic digester is necessary to accurately model and predict the reactor performance, especially at a larger scale operation. A lab-scale (3.78 l) and a pilot-scale (120 l) anaerobic digester were operated at both mixing and non-mixing conditions. At lab-scale no significant difference in performance was found between these conditions. In each case about 0.25 lCH4/lreactor/d of biogas was produced. The model predictions were in close agreement with measured values. At pilot-scale, however, the influence of mixing became important. A reduction of about 10% of methane production occurred during unmixed conditions. Furthermore also a build-up of volatile fatty acids (up to 3 gCOD/l) prevailed. This behavior could not be predicted by using a CSTR approach. In contrast, it was accurately predicted with the proposed model, which includes a more rigorous mixing next to common reaction kinetics. Prediction of the daily biogas production assuming a perfectly mixed reactor revealed an overestimation of the biogas production by 10%. It is therefore recommended to use more accurate mixing models in order to predict biogas production from anaerobic digesters.
Journal: Chemical Engineering Journal - Volume 255, 1 November 2014, Pages 71–77