| Title: | Developing a vacuum thermal stripping - acid absorption process for ammonia recovery from anaerobic digester effluent |
| Address: | "Department of Environmental Resources Engineering, College of Environmental Science and Forestry, State University of New York, 1 Forestry Dr., Syracuse, NY 13210, USA. Department of Environmental Resources Engineering, College of Environmental Science and Forestry, State University of New York, 1 Forestry Dr., Syracuse, NY 13210, USA. Electronic address: wtao@esf.edu" |
| DOI: | 10.1016/j.watres.2016.09.054 |
| ISSN/ISBN: | 1879-2448 (Electronic) 0043-1354 (Linking) |
| Abstract: | "To prevent acetoclastic methanogens from ammonia inhibition in anaerobic digestion of protein-rich substrates, ammonia needs to be removed or recovered from digestate. This paper presents an innovative ammonia recovery process that couples vacuum thermal stripping with acid absorption. Ammonia is stripped out of digestate boiling at a temperature below the normal boiling point due to vacuum. Stripped ammonia is absorbed to a sulfuric acid solution, forming ammonium sulfate crystals as a marketable product. Three common types of digestate were found to have boiling point temperature-vacuum curves similar to water. Seven combinations of boiling temperature and vacuum (50 degrees C 16.6 kPa, 58 degrees C 20.0 kPa, 65 degrees C 25.1 kPa, 70 degrees C 33.6 kPa, 80 degrees C 54.0 kPa, 90 degrees C 74.2 kPa, and 100 degrees C 101.3 kPa) were tested for batch stripping of ammonia in dairy manure digestate. 93.3-99.9% of ammonia was stripped in 3 h. The Lewis-Whitman model fitted ammonia stripping process well. Ammonia mass transfer coefficient was significantly higher at boiling temperature 65-100 degrees C and vacuum pressure 25.1-101.3 kPa than 50-58 degrees C and 16.6-20.0 kPa. The low ammonia saturation concentrations (0-24 mg N/L) suggested a large driving force to strip ammonia. The optimum boiling point temperature - vacuum pressure for ammonia recovery in a recirculation line of a mesophilic digester was 65 degrees C and 25.1 kPa, at which the ammonia mass transfer coefficient was as high as 37.3 mm/h. Installation of a demister and liquid trap could avoid negative effects of higher stripping temperature and stronger vacuum on formation of ammonium sulfate crystals. Pilot tests demonstrated that high-purity ammonium sulfate crystals could be produced by controlling sulfuric acid content and maintaining acid solution saturated with ammonium sulfate. Although volatile organic compounds such as cyclohexene were found in the final acid solutions, no volatile organic compounds were found in the recovered crystals" |
| Keywords: | *Ammonia *Manure Temperature Vacuum Ammonium sulfate Anaerobic digestion Boiling point Dairy manure Mass transfer coefficient Temperature-vacuum curve; |
| Notes: | "MedlineUkwuani, Anayo T Tao, Wendong eng England 2016/10/05 Water Res. 2016 Dec 1; 106:108-115. doi: 10.1016/j.watres.2016.09.054. Epub 2016 Sep 27" |
