Supercritical water oxidation of phenol and 2,4 dinitrophenol

The destruction kinetics of two model compounds has been investigated in the University of British Columbia (UBC) Supercritical Water Oxidation (SCWO) pilot plant. High concentrations of phenol (2.7% and 4% by weight) were oxidized at pressures of 24 to 26 MPa, temperatures of 666 to 778 K, and 0 to...

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Main Author: Perez, Ivette Vera
Language:English
Published: 2009
Online Access:http://hdl.handle.net/2429/13638
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spelling ndltd-LACETR-oai-collectionscanada.gc.ca-BVAU.2429-136382014-03-14T15:46:54Z Supercritical water oxidation of phenol and 2,4 dinitrophenol Perez, Ivette Vera The destruction kinetics of two model compounds has been investigated in the University of British Columbia (UBC) Supercritical Water Oxidation (SCWO) pilot plant. High concentrations of phenol (2.7% and 4% by weight) were oxidized at pressures of 24 to 26 MPa, temperatures of 666 to 778 K, and 0 to 39% oxygen excess. Phenol and Total Organic Carbon (TOC) conversions varied from 92 to 99.98% and 75 to 99.77% respectively. The second group of wastes studied contained 2,4 dinitrophenol (DNP). Two different solutions that simulated an aromatic nitration facility's wash-water were investigated. The first one contained 2.4% by wt. 2,4 dinitrophenol with 2% by wt. ammonium sulphate and simulated the final wash waters from the nitration plant with no sulphates elimination. The second solution contained 2.27% by wt. as ammonium dinitrophenol, with no sulphates. For the first DNP waste, at process conditions of 25 MPa, 780 K and 37% oxygen excess, 99.9996% destruction efficiencies were obtained for 2,4 dinitrophenol, and 99.92% for TOC. Mono-nitrophenols were detected as intermediates, but not in the liquid effluent, where residuals of ammonium bicarbonate and sulphates were detected. No NO[sub x] or CO was present in the gaseous effluent streams. This solution resulted to be very corrosive to the system. The second solution was treated at 22.9 ±0.1 MPa, 742-813 K and oxygen concentrations ranging from sub-stoichiometric to 69% excess. Destruction efficiencies for 2,4 dinitrophenol were 99.9996% in all cases (not detected). TOC destruction efficiencies ranged from 98.98 to 99.98%, while ammonia destruction ranged from 15 to 50%. Picric acid, mono-nitrophenols, ammonium carbonate and bicarbonate were detected as intermediates, but not in the liquid effluent. No CO or NO[sub x] was present in the effluent gas samples, except in cases with less than stoichiometric oxygen. 2009-10-05T21:40:29Z 2009-10-05T21:40:29Z 2002 2009-10-05T21:40:29Z 2002-11 Electronic Thesis or Dissertation http://hdl.handle.net/2429/13638 eng UBC Retrospective Theses Digitization Project [http://www.library.ubc.ca/archives/retro_theses/]
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language English
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description The destruction kinetics of two model compounds has been investigated in the University of British Columbia (UBC) Supercritical Water Oxidation (SCWO) pilot plant. High concentrations of phenol (2.7% and 4% by weight) were oxidized at pressures of 24 to 26 MPa, temperatures of 666 to 778 K, and 0 to 39% oxygen excess. Phenol and Total Organic Carbon (TOC) conversions varied from 92 to 99.98% and 75 to 99.77% respectively. The second group of wastes studied contained 2,4 dinitrophenol (DNP). Two different solutions that simulated an aromatic nitration facility's wash-water were investigated. The first one contained 2.4% by wt. 2,4 dinitrophenol with 2% by wt. ammonium sulphate and simulated the final wash waters from the nitration plant with no sulphates elimination. The second solution contained 2.27% by wt. as ammonium dinitrophenol, with no sulphates. For the first DNP waste, at process conditions of 25 MPa, 780 K and 37% oxygen excess, 99.9996% destruction efficiencies were obtained for 2,4 dinitrophenol, and 99.92% for TOC. Mono-nitrophenols were detected as intermediates, but not in the liquid effluent, where residuals of ammonium bicarbonate and sulphates were detected. No NO[sub x] or CO was present in the gaseous effluent streams. This solution resulted to be very corrosive to the system. The second solution was treated at 22.9 ±0.1 MPa, 742-813 K and oxygen concentrations ranging from sub-stoichiometric to 69% excess. Destruction efficiencies for 2,4 dinitrophenol were 99.9996% in all cases (not detected). TOC destruction efficiencies ranged from 98.98 to 99.98%, while ammonia destruction ranged from 15 to 50%. Picric acid, mono-nitrophenols, ammonium carbonate and bicarbonate were detected as intermediates, but not in the liquid effluent. No CO or NO[sub x] was present in the effluent gas samples, except in cases with less than stoichiometric oxygen.
author Perez, Ivette Vera
spellingShingle Perez, Ivette Vera
Supercritical water oxidation of phenol and 2,4 dinitrophenol
author_facet Perez, Ivette Vera
author_sort Perez, Ivette Vera
title Supercritical water oxidation of phenol and 2,4 dinitrophenol
title_short Supercritical water oxidation of phenol and 2,4 dinitrophenol
title_full Supercritical water oxidation of phenol and 2,4 dinitrophenol
title_fullStr Supercritical water oxidation of phenol and 2,4 dinitrophenol
title_full_unstemmed Supercritical water oxidation of phenol and 2,4 dinitrophenol
title_sort supercritical water oxidation of phenol and 2,4 dinitrophenol
publishDate 2009
url http://hdl.handle.net/2429/13638
work_keys_str_mv AT perezivettevera supercriticalwateroxidationofphenoland24dinitrophenol
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