Solubility and Phase Diagram for the Ternary Sodium Oxalate + Hydrogen Peroxide + Water System at (283.15 and 293.15) K

2007 ◽  
Vol 52 (3) ◽  
pp. 863-865
Author(s):  
Hong-Kun Zhao ◽  
Dao-Sen Zhang ◽  
Cao Tang ◽  
Rong-Rong Li ◽  
Ming-Li Su ◽  
...  
Keyword(s):  
Phase Diagram ◽  
Hydrogen Peroxide ◽  
Water System ◽  
Sodium Oxalate

Solubility and Phase Diagram of the Quaternary Sodium Carbonate + Ethanol + Hydrogen Peroxide + Water System atT= 293.15 K

2007 ◽  
Vol 52 (4) ◽  
pp. 1213-1216
Author(s):  
Hong-kun Zhao ◽  
Rong-rong Li ◽  
Ming-li Su ◽  
Cao Tang ◽  
Dao-sen Zhang ◽  
...  
Keyword(s):  
Phase Diagram ◽  
Hydrogen Peroxide ◽  
Sodium Carbonate ◽  
Water System

(Solid + Liquid) Phase Diagram for the Ternary Potassium Oxalate + Hydrogen Peroxide + Water System at 283.15 K and 293.15 K

2007 ◽  
Vol 52 (1) ◽  
pp. 44-46
Author(s):  
Hong-Kun Zhao ◽  
Dao-Sen Zhang ◽  
Cao Tang ◽  
Rong-Rong Li ◽  
Wen-Lin Xu ◽  
...  
Keyword(s):  
Phase Diagram ◽  
Hydrogen Peroxide ◽  
Liquid Phase ◽  
Water System ◽  
Potassium Oxalate ◽  
Solid Liquid

Study of the Phase Diagram of the CTAB/Benzyl Alcohol/Water System

1995 ◽  
Vol 172 (2) ◽  
pp. 494-501 ◽  
Author(s):  
Gemma Montalvo ◽  
Mercedes Valiente ◽  
Elvira Rodenas
Keyword(s):  
Phase Diagram ◽  
Benzyl Alcohol ◽  
Water System ◽  
Alcohol Water

Lyotropic mesomorphism of the cesium pentadecafluorooctanoate/water system: high-resolution phase diagram

1987 ◽  
Vol 91 (15) ◽  
pp. 4092-4105 ◽  
Author(s):  
Neville. Boden ◽  
Simon A. Corne ◽  
Kenneth W. Jolley
Keyword(s):  
Phase Diagram ◽  
High Resolution ◽  
Water System

Combining UASB technology and advanced oxidation processes (AOPs) to treat food processing wastewaters

2002 ◽  
Vol 45 (10) ◽  
pp. 329-334 ◽  
Author(s):  
G.O. Sigge ◽  
T.J. Britz ◽  
P.C. Fourie ◽  
C.A. Barnardt ◽  
R. Strydom
Keyword(s):  
Hydrogen Peroxide ◽  
Food Processing ◽  
Advanced Oxidation Processes ◽  
Water System ◽  
Post Treatment ◽  
Significant Progress ◽  
Oxidation Processes ◽  
Legal Limit ◽  
Direct Discharge ◽  
Made In

UASB treatment of fruit cannery and winery effluents was shown to be feasible. However, the treated effluents still have residual COD levels well above the legal limit of 75 mg.L−1 for direct discharge to a water system and a form of post-treatment is necessary to reduce the COD further. Ozone and ozone/hydrogen peroxide were used in combination with a granular activated carbon contacting column to assess the effectiveness as a post-treatment option for the UASB treated fruit cannery and winery effluent. Colour reduction in the effluents ranged from 66 to 90% and COD reductions of 27–55% were achieved. The combination of ozone and hydrogen peroxide gave better results than ozonation alone. Significant progress was thus made in achieving the legal limit of 75 mg.L−1.

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