{"id":{"repo_id":"uiuc","oai_identifier":"oai:www.ideals.illinois.edu:2142/18259"},"canonical_url":"https://search.dev.ndltd.org/etd/uiuc/oai:www.ideals.illinois.edu:2142/18259","repository":{"repo_id":"uiuc","name":"University of Illinois - Urbana-Champaign","base_url":"https://www.ideals.illinois.edu/oai-pmh"},"display":{"title":"Comparing the responses of nitrifiers to differing ammonia loadings","abstract":"Return active sludge from the Danville Sanitary plant (Danville, IL) was fed 10 mg NH3-N/L per cycle of separated swine manure to allow the biomass to adapt to a new influent in a sequencing batch reactor. The biomass was then separated into three reactors. A control reactor was exposed to 10 mg NH3-N/L . A medium stress reactor was exposed to ammonia loading increasing from 10 mg NH3-N/L to 120 mg NH3-N/L. A final high stress reactor was exposed to the same increasing loading as the medium stress reactor with periodic shock loads. Biomass was regularly taken from each reactor and batch respirometer tests were performed with initial ammonia loading varying from 20 mg NH3-N/L to 550 mg NH3-N/L. Modifications to Activated Sludge Model 3 (ASM3) were used to attempt to model the OUR curves generated, but the curves could not be fitted. Despite the inability to model the OUR curves, the biomass from each reactor was found to have qualitatively different OUR curves from each other.","abstract_html":"Return active sludge from the Danville Sanitary plant (Danville, IL) was fed 10 mg NH3-N/L per cycle of separated swine manure to allow the biomass to adapt to a new influent in a sequencing batch reactor. The biomass was then separated into three reactors. A control reactor was exposed to 10 mg NH3-N/L . A medium stress reactor was exposed to ammonia loading increasing from 10 mg NH3-N/L to 120 mg NH3-N/L. A final high stress reactor was exposed to the same increasing loading as the medium stress reactor with periodic shock loads. Biomass was regularly taken from each reactor and batch respirometer tests were performed with initial ammonia loading varying from 20 mg NH3-N/L to 550 mg NH3-N/L. Modifications to Activated Sludge Model 3 (ASM3) were used to attempt to model the OUR curves generated, but the curves could not be fitted. Despite the inability to model the OUR curves, the biomass from each reactor was found to have qualitatively different OUR curves from each other.","abstract_has_math":false,"creators":["Anderson, Blake W."],"institution":"University of Illinois at Urbana-Champaign","degree_name":"M.S.","degree_level":"Thesis","degree_discipline":"Environ Engr in Civil Engr","degree_department":null,"school":null,"contributors":["Morgenroth, Eberhard F."],"advisors":[],"committee_chairs":[],"committee_members":[],"year":2011,"date_issued":"2011-01-14T22:41:54Z","date_published":"2011-01-14T22:41:54Z","updated_at":"2026-07-22T22:25:11Z","subjects":["Nitrifier Modeling","Ammonia acclimation"],"languages":["en"],"rights":["Copyright 2010 Blake W. Anderson"],"rights_urls":[],"identifier_entries":[]},"links":{"outbound_url":"http://hdl.handle.net/2142/18259","outbound_label":"Handle","outbound_source":"dc:identifier"},"metadata_groups":[{"id":"people","label":"People","entries":[{"key":"dc:contributor","label":"Contributor","values":["Morgenroth, Eberhard F."]},{"key":"dc:creator","label":"Author","values":["Anderson, Blake W."]}]},{"id":"academic_context","label":"Academic Context","entries":[{"key":"dc:date","label":"Dc Date","values":["2011-01-14T22:41:54Z","2013-01-20T11:00:11Z","2010-12"]},{"key":"thesis:degree_discipline","label":"Discipline","values":["Environ Engr in Civil Engr"]},{"key":"thesis:degree_level","label":"Degree Level","values":["Thesis"]},{"key":"thesis:degree_name","label":"Degree Name","values":["M.S."]},{"key":"thesis:institution_name","label":"Thesis Institution Name","values":["University of Illinois at Urbana-Champaign"]}]},{"id":"subjects_keywords","label":"Subjects and Keywords","entries":[{"key":"dc:subject","label":"Dc Subject","values":["Nitrifier Modeling","Ammonia acclimation"]}]},{"id":"language_rights","label":"Language and Rights","entries":[{"key":"dc:language","label":"Dc Language","values":["en"]},{"key":"dc:rights","label":"Dc Rights","values":["Copyright 2010 Blake W. 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Modifications to Activated Sludge Model 3 (ASM3) were used to attempt to model the OUR curves generated, but the curves could not be fitted. Despite the inability to model the OUR curves, the biomass from each reactor was found to have qualitatively different OUR curves from each other.","Item withdrawn by Mark Zulauf (zulauf@illinois.edu) on 2010-11-15T15:02:14Z Item was in collections: University of Illinois Theses & Dissertations (ID: 1) No. of bitstreams: 21 Smoothed Data in Text Files.zip: 1718548 bytes, checksum: 7c28e9b2ef0f99c8978f110d43a1f83d (MD5) Smooth Data and Aquasim fit files for every Respirometer Cell.zip: 83038951 bytes, checksum: d3f2bde748b4e66bfbf553c40799adde (MD5) SBR Operating Data.xlsx: 81559 bytes, checksum: 52b48cf3e45e57849e6e6e9ec30ac52f (MD5) Raw Respirometer Data.zip: 581768 bytes, checksum: cc02b8ad7a0a2736625e8ca621854430 (MD5) Parameter Fitting Forced for every Respirometer Cell.zip: 85061614 bytes, checksum: a21dd5fcebf2a5b837fe9140e7a0a2c7 (MD5) Model Data Used For V Shaped Graph.xlsx: 101397 bytes, checksum: 115214643a1865722bafa5bb3852d2bc (MD5) Kinetic Parameters Trying to each test to have the same parameters.xlsx: 133348 bytes, checksum: 3e87f5d77a41b58b00bcd8b7af521a48 (MD5) Kinetic Parameters Each Cell individually fit.xlsx: 133240 bytes, checksum: 12a9419f444790706c8d9593e74e4ab9 (MD5) Graphes for Qualitative Analysis.xlsx: 914077 bytes, checksum: 6b6eb3ba4a79f21c8ad3b200b65dbabb (MD5) Charts in Thesis-Parameter fitting 2.xlsx: 135636 bytes, checksum: cc103e30370d98a40b5f2edf68eabe78 (MD5) Charts in Thesis-Parameter fitting 1.xlsx: 135245 bytes, checksum: ce2145346ffc98cb67854b854491cf41 (MD5) Appendix Graph 8_1s react cell all.xlsx: 215434 bytes, checksum: 4c28fceb9bd7695ee2496e269b0eacf1 (MD5) Appendix Graph 7_27c react cell all.xlsx: 643966 bytes, checksum: d44820c516b16801d15c503353e5ef69 (MD5) Appendix Graph 7_25g react cell all.xlsx: 553888 bytes, checksum: 8432068ec7e8136d89632a5d712b5b61 (MD5) Appendix Graph 7_22s react cell all.xlsx: 611928 bytes, checksum: 2402db098b78eb3729f77e76bc76c867 (MD5) Appendix Graph 7_19g react cell all.xlsx: 649662 bytes, checksum: 23e4497e2076c4f3ff0984190086c00c (MD5) Appendix Graph 7_7c react cell all.xlsx: 596596 bytes, checksum: c3ffa5aa706290c057a285e3812196e8 (MD5) Appendix Graph 7_3g react cell all.xlsx: 495364 bytes, checksum: 29d33ed0380660bd48938c83e9850dce (MD5) Appendix Graph 7_2s react cell all.xlsx: 373985 bytes, checksum: dff6eea11cd653a5d822b6e25c1b40da (MD5) Appendix Graph 6_11s react cell All.xlsx: 559159 bytes, checksum: 9d7bf9392898f408ab1eea6bbb319ebe (MD5) Anderson_Blake.pdf: 1064801 bytes, checksum: 81f4e39a8398d5427a3b8bf9be628564 (MD5)","Made available in DSpace on 2011-01-14T22:41:54Z (GMT). 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Anderson"],"dc:subject":["Nitrifier Modeling","Ammonia acclimation"],"dc:title":["Comparing the responses of nitrifiers to differing ammonia loadings"],"thesis:degree_discipline":["Environ Engr in Civil Engr"],"thesis:degree_level":["Thesis"],"thesis:degree_name":["M.S."],"thesis:institution_name":["University of Illinois at Urbana-Champaign"]},"updated_at":"2026-07-22T22:25:11Z"}