scholarly journals Supercritical water oxidation of phenol and process enhancement with in situ formed Fe2O3 nano catalyst

Author(s):  
Ammar Al-Atta ◽  
Farooq Sher ◽  
Abu Hazafa ◽  
Ayesha Zafar ◽  
Hafiz M. N. Iqbal ◽  
...  

AbstractDuring the past few decades, the treatment of hazardous waste and toxic phenolic compounds has become a major issue in the pharmaceutical, gas/oil, dying, and chemical industries. Considering polymerization and oxidation of phenolic compounds, supercritical water oxidation (SCWO) has gained special attention. The present study objective was to synthesize a novel in situ Fe2O3nano-catalyst in a counter-current mixing reactor by supercritical water oxidation (SCWO) method to evaluate the phenol oxidation and COD reduction at different operation conditions like oxidant ratios and concentrations. Synthesized nano-catalyst was characterized by powder X-ray diffraction (XRD) and transmission electron microscope (TEM). TEM results revealed the maximum average particle size of 26.18 and 16.20 nm for preheated and non-preheated oxidant configuration, respectively. XRD showed the clear peaks of hematite at a 2θ value of 24, 33, 35.5, 49.5, 54, 62, and 64 for both catalysts treated preheated and non-preheated oxidant configurations. The maximum COD reduction and phenol oxidation of about 93.5% and 99.9% were observed at an oxidant ratio of 1.5, 0.75 s, 25 MPa, and 380 °C with a non-preheated H2O2 oxidant, while in situ formed Fe2O3nano-catalyst showed the maximum phenol oxidation of 99.9% at 0.75 s, 1.5 oxidant ratio, 25 MPa, and 380 °C. Similarly, in situ formed Fe2O3 catalyst presented the highest COD reduction of 97.8% at 40 mM phenol concentration, 1.0 oxidant ratio, 0.75 s residence time, 380 °C, and 25 MPa. It is concluded and recommended that SCWO is a feasible and cost-effective alternative method for the destruction of contaminants in water which showed the complete conversion of phenol within less than 1 s and 1.5 oxidant ratio.

2019 ◽  
Vol 80 (4) ◽  
pp. 620-633 ◽  
Author(s):  
Huiwen Zhang ◽  
Xiaoman Zhang ◽  
Lei Ding ◽  
Miao Gong ◽  
Ying Su ◽  
...  

Abstract The treatment of toxic and difficult-to-degrade phenolic compounds has become a key issue in the coking, pharmaceutical, and chemical industries. Considering the polymerization and oxidation of phenolic compounds in supercritical water partial oxidation/supercritical water oxidation (SCWPO/SCWO), the present study reviewed the removal efficiency and reaction pathway of phenolic compounds and phenolic waste/wastewater under different reaction conditions. Temperature is the dominant factor affecting the SCWO reaction. When the oxidizing ability is insufficient, the organics polymerize to form phenolic compounds. The gradual increase of oxidant equivalent causes the intermediate product to gradually oxidize to CO2 and H2O completely. Finally, the free radical reaction mechanism is considered to be a typical SCWO reaction mechanism.


RSC Advances ◽  
2016 ◽  
Vol 6 (59) ◽  
pp. 54202-54214 ◽  
Author(s):  
Hongzhen Chen ◽  
Guangwei Wang ◽  
Yuanjian Xu ◽  
Zhong Chen ◽  
Fengjun Yin

Red mud was used in the supercritical water oxidation (SCWO) disposal of sewage sludge, not only as a neutralizer for acidic substances produced in situ, but also as a catalyst for decomposition of pollutants.


2012 ◽  
Vol 65 (11) ◽  
pp. 2034-2041
Author(s):  
F. Takahashi ◽  
Z. R. Sun ◽  
K. Fukushi ◽  
Y. Oshima ◽  
K. Yamamoto

For practical applications of supercritical water oxidation to wastewater treatment, the deposition of inorganic salts in supercritical phase must be controlled to prevent a reactor from clogging. This study investigated enhanced removal of sodium salts with titanium particles, serving as a salt trapper and a catalyst precursor, and sodium recovery by sub-critical water. When Na2CO3 was tested as a model salt, sodium removal efficiency was higher than theoretically maximum efficiency defined by Na2CO3 solubility. The enhanced sodium removal resulted from in-situ synthesis of sodium titanate, which could catalyse acetic acid oxidation. The kinetics of sodium removal was described well by a diffusion mass-transfer model combined with a power law-type rate model of sodium titanate synthesis. Titanium particles showed positive effect on sodium removal in the case of NaOH, Na2SO4 and Na3PO4. However, they had negligible effect for NaCl and negative effect for Na2CrO4, respectively. More than 99% of trapped sodium was recovered by sub-critical water except for Na2CrO4. In contrast, sodium recovery efficiency remained less than 50% in the case of Na2CrO4. Reused titanium particles showed the same performance for enhanced sodium removal. Enhanced salt removal supported by in-situ catalyst synthesis has great potential to enable both salt removal control and catalytic oxidation.


1996 ◽  
Author(s):  
Steven F. Rice ◽  
Richard R. Steeper ◽  
Russell G. Hanush ◽  
Jason D. Aiken ◽  
Eric Croiset

1995 ◽  
Author(s):  
Steven F. Rice ◽  
Jefferson W. Tester ◽  
Kenneth Brezinsky

1995 ◽  
Author(s):  
Steven F. Rice ◽  
Jefferson W. Tester ◽  
Kenneth Brezinsky

2011 ◽  
Vol 4 (3) ◽  
pp. 219-230 ◽  
Author(s):  
Angel Martin ◽  
Maria Dolores Bermejo ◽  
Maria Jose Cocero

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