Optimization of VFA production in an atad reactor with respect to aeration rates and removal of phosphorus, incorporating a magnesium ammonium phosphate (map) crystallizer from the atad supernatant
Previous researchers have demonstrated that a mixture of primary and secondary sludge provides increased production of VFA in ATAD. Experiments were carried out at the UBC pilot plant, in two phases, using a 35/65 mixture of primary/secondary sludge, to determine the optimum aeration rate with re...
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ndltd-LACETR-oai-collectionscanada.gc.ca-BVAU.2429-92602014-03-14T15:43:17Z Optimization of VFA production in an atad reactor with respect to aeration rates and removal of phosphorus, incorporating a magnesium ammonium phosphate (map) crystallizer from the atad supernatant Sharma, Abyartha Previous researchers have demonstrated that a mixture of primary and secondary sludge provides increased production of VFA in ATAD. Experiments were carried out at the UBC pilot plant, in two phases, using a 35/65 mixture of primary/secondary sludge, to determine the optimum aeration rate with respect to production/generation of VFA, and to investigate the removal of phosphorus by forced formation of struvite in an upflow crystallizer. The source sludge for the research was obtained from an on-site modified UCT process, and mixed in the correct ratios prior to feeding on an hourly basis to the 125-L tanks. The tanks, were configured in parallel and operated as individual first stage reactors, one of which was the control tank. During the first stage, the control tank was maintained at a constant aeration rate of 50 ml/min (as suggested by EPA). The aeration rate in the test tank was varied from 0 ml/min (nitrogen was supplied) to 100 ml/min, at increments of 25 ml/min. Throughout the entire experimental period, temperatures were in the thermophilic range, between 47°C and 58°C inside the tanks; feed solids were maintained around 1.4% TSS, and ORP was consistent between -300 mV and -450 mV. There was higher production of VFA at lower aeration rates, the highest occurring when 25 ml/min air was supplied. Analysis of nutrients confirmed that there was a high release of stored phosphorus and an increase in ammonia nitrogen. The ratio of VFA: PO₄-P was the highest when 25 ml/min air was supplied. 2009-06-16T17:26:08Z 2009-06-16T17:26:08Z 1999 2009-06-16T17:26:08Z 1999-11 Electronic Thesis or Dissertation http://hdl.handle.net/2429/9260 eng UBC Retrospective Theses Digitization Project [http://www.library.ubc.ca/archives/retro_theses/] |
collection |
NDLTD |
language |
English |
sources |
NDLTD |
description |
Previous researchers have demonstrated that a mixture of primary and secondary
sludge provides increased production of VFA in ATAD. Experiments were carried out at
the UBC pilot plant, in two phases, using a 35/65 mixture of primary/secondary sludge,
to determine the optimum aeration rate with respect to production/generation of VFA,
and to investigate the removal of phosphorus by forced formation of struvite in an upflow
crystallizer. The source sludge for the research was obtained from an on-site
modified UCT process, and mixed in the correct ratios prior to feeding on an hourly basis
to the 125-L tanks. The tanks, were configured in parallel and operated as individual first
stage reactors, one of which was the control tank.
During the first stage, the control tank was maintained at a constant aeration rate
of 50 ml/min (as suggested by EPA). The aeration rate in the test tank was varied from 0
ml/min (nitrogen was supplied) to 100 ml/min, at increments of 25 ml/min. Throughout
the entire experimental period, temperatures were in the thermophilic range, between
47°C and 58°C inside the tanks; feed solids were maintained around 1.4% TSS, and ORP
was consistent between -300 mV and -450 mV. There was higher production of VFA
at lower aeration rates, the highest occurring when 25 ml/min air was supplied. Analysis
of nutrients confirmed that there was a high release of stored phosphorus and an increase
in ammonia nitrogen. The ratio of VFA: PO₄-P was the highest when 25 ml/min air was
supplied. |
author |
Sharma, Abyartha |
spellingShingle |
Sharma, Abyartha Optimization of VFA production in an atad reactor with respect to aeration rates and removal of phosphorus, incorporating a magnesium ammonium phosphate (map) crystallizer from the atad supernatant |
author_facet |
Sharma, Abyartha |
author_sort |
Sharma, Abyartha |
title |
Optimization of VFA production in an atad reactor with respect to aeration rates and removal of phosphorus, incorporating a magnesium ammonium phosphate (map) crystallizer from the atad supernatant |
title_short |
Optimization of VFA production in an atad reactor with respect to aeration rates and removal of phosphorus, incorporating a magnesium ammonium phosphate (map) crystallizer from the atad supernatant |
title_full |
Optimization of VFA production in an atad reactor with respect to aeration rates and removal of phosphorus, incorporating a magnesium ammonium phosphate (map) crystallizer from the atad supernatant |
title_fullStr |
Optimization of VFA production in an atad reactor with respect to aeration rates and removal of phosphorus, incorporating a magnesium ammonium phosphate (map) crystallizer from the atad supernatant |
title_full_unstemmed |
Optimization of VFA production in an atad reactor with respect to aeration rates and removal of phosphorus, incorporating a magnesium ammonium phosphate (map) crystallizer from the atad supernatant |
title_sort |
optimization of vfa production in an atad reactor with respect to aeration rates and removal of phosphorus, incorporating a magnesium ammonium phosphate (map) crystallizer from the atad supernatant |
publishDate |
2009 |
url |
http://hdl.handle.net/2429/9260 |
work_keys_str_mv |
AT sharmaabyartha optimizationofvfaproductioninanatadreactorwithrespecttoaerationratesandremovalofphosphorusincorporatingamagnesiumammoniumphosphatemapcrystallizerfromtheatadsupernatant |
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1716651665071800320 |