Effects of Mixing Duration on Biogas Production and Methanogen Distribution in Dairy Manure Anaerobic Digesters

Animal Manure Management April 30, 2015 Print Friendly and PDF

Why Did We Study Mixing Duration?

Mixing is an important parameter for anaerobic digesters for both design and operation. This is especially true for digesters that treat diary manure, which is a mixture of feces, urine, blood, food wastes, and bedding. Many of the solids fed to the digester have no or low degradability, and some of the large fibers can clog pumps or pipes in the transfer system. Mixing also plays an important role in maintaining a uniform environment for biological processes. However, the energy input for operating mechanical mixers requires a large part of the total energy for a biogas plant. Previous studies have suggested that optimum biogas production does not require continuous active mixing. It is essential to evaluate the mixing duration in order to balance energy inputs and biogas production rates.

What Did We Do?

The study was designed as a one factor (mixing duration) experiment with three levels and was carried out in triplicates. Three pilot scale anaerobic digesters were used to compare the impact of different mixing duration (continuous - CON, intermittent - INT, and no mixing - NO) on the performance of biogas production from dairy manure, Figure 1.

Figure 1. a laboratory scale digester

Figure 1: Digester Design

During the experiment, all digesters were fed 8 kg of dairy manure daily (total solid content = 5.5%), and operated at 37oC with a hydraulic retention time (HRT) of 21 days.  The mixing and feeding were controlled by an automated computer system, Figure 2. Mixers were set at a speed of 450 revolution per min (RPM). Biogas production was recorded three times a week and the percentage of methane content was analyzed weekly. Manure samples were collected weekly from the feed tank, top, middle & bottom of the digester, and from the effluent tank for volatile solids (VS), chemical oxygen demand (COD), pH, carbon to nitrogen ratio (C/N), and violate fatty acids (VFAs).  The concentration of archea and five common methanogens found in digesters was also determined using quantitative polymerase chain reaction (qPCR).

Figure 2. A closeup of the top of the lab-scale digester

Figure 2: Digester Mixing System

What Have We Learned?

The cumulative biogas production from digesters with no mixing was statistically significantly higher than intermittent and continuous (CON) mixing at the same loading rate. However, CON had a higher methane production rate per kg of volatile solids destroyed, Figure 3.

Figure 3: Methane Production Rate per Volatile Solids Destroyed 

Future Plans

We are currently exploring the settling of manure solids in digesters with different mixing duration through a tracer study. The impact of different settling time on the hydraulic retention time (HRT), would help us better understand the performance of the anaerobic digesters with different mixing duration.

Authors

Hui Wang, Graduate Research Assistant, University of Wisconsin-Madison, hwang355@wisc.edu

Rebecca A. Larson, Assistant Professor and Extension Specialist, University of Wisconsin-Madison, ralarson2@wisc.edu

Acknowledgements

This material is based upon work supported by the National Institute of Food and Agriculture, United States Department of Agriculture, under ID number WIS01693. 

Institute for Environmentally Integrated Dairy Management (Marshfield, WI), United States Dairy Forage Research Center

The authors are solely responsible for the content of these proceedings. The technical information does not necessarily reflect the official position of the sponsoring agencies or institutions represented by planning committee members, and inclusion and distribution herein does not constitute an endorsement of views expressed by the same. Printed materials included herein are not refereed publications. Citations should appear as follows. EXAMPLE: Authors. 2015. Title of presentation. Waste to Worth: Spreading Science and Solutions. Seattle, WA. March 31-April 3, 2015. URL of this page. Accessed on: today’s date.

 

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USDA / NIFA

This work is supported by the USDA National Institute of Food and Agriculture, New Technologies for Ag Extension project.