TY - JOUR
T1 - TCAA degradation in ultraviolet (UV) irradiation/hydrogen peroxide (H 2O2)/micro-aeration (MCA) combination process
AU - Gao, N. Y.
AU - Chu, W. H.
AU - Deng, Y.
AU - Xu, B.
PY - 2009
Y1 - 2009
N2 - The photochemical degradation of trichloroacetic acid (TCAA) employing ultraviolet (UV) irradiation/hydrogen peroxide (H2O 2)/micro-aeration (MCA) combination process was investigated by varying operational parameters. Relatively slow TCAA degradation was observed during direct UV radiation and H2O2 oxidation, while TCAA cannot be removed by MCA alone. UV/H2O2/MCA combination process proved to be more effective than UV/H2O2. With the initial concentration of 55.7 μgl-1, more than 93.4% of TCAA can be removed within 180 min under UV radiation intensity of 1,048.7 μW cm -2, H2O2 dosage of 30mgl-1 and MCA flow rate of 25 l min-1 in neutral conditions. Removal rate of TCAA was sensitive to UV radiation intensity, H2O2 dose and solution pH, but appeared to be slightly influenced by initial TCAA concentration. There was a higher correlation between pseudo-first rate constant k and UV intensity and H2O2 dosage, implying that higher removal capacity can be achieved by improvement of both factors. The newly found trichloroacetamide (TCAcAm), the potential TCAA, was more frangible than TCAA, indicating that TCAA hardly regenerates by hydrolysis of TCAcAm. Finally, a preliminary cost analysis revealed that the UV/H2O2/MCA process was more cost-effective than the UV/H2O2 process in removal of TCAA from drinking water.
AB - The photochemical degradation of trichloroacetic acid (TCAA) employing ultraviolet (UV) irradiation/hydrogen peroxide (H2O 2)/micro-aeration (MCA) combination process was investigated by varying operational parameters. Relatively slow TCAA degradation was observed during direct UV radiation and H2O2 oxidation, while TCAA cannot be removed by MCA alone. UV/H2O2/MCA combination process proved to be more effective than UV/H2O2. With the initial concentration of 55.7 μgl-1, more than 93.4% of TCAA can be removed within 180 min under UV radiation intensity of 1,048.7 μW cm -2, H2O2 dosage of 30mgl-1 and MCA flow rate of 25 l min-1 in neutral conditions. Removal rate of TCAA was sensitive to UV radiation intensity, H2O2 dose and solution pH, but appeared to be slightly influenced by initial TCAA concentration. There was a higher correlation between pseudo-first rate constant k and UV intensity and H2O2 dosage, implying that higher removal capacity can be achieved by improvement of both factors. The newly found trichloroacetamide (TCAcAm), the potential TCAA, was more frangible than TCAA, indicating that TCAA hardly regenerates by hydrolysis of TCAcAm. Finally, a preliminary cost analysis revealed that the UV/H2O2/MCA process was more cost-effective than the UV/H2O2 process in removal of TCAA from drinking water.
KW - Advanced oxidation processes
KW - Cost analysis
KW - Disinfection by-products
KW - Microaeration
KW - Trichloroacetamide
KW - Trichloroacetic acid
UR - http://www.scopus.com/inward/record.url?scp=77149133779&partnerID=8YFLogxK
U2 - 10.2166/aqua.2009.005
DO - 10.2166/aqua.2009.005
M3 - Article
AN - SCOPUS:77149133779
SN - 0003-7214
VL - 58
SP - 510
EP - 518
JO - Journal of Water Supply: Research and Technology - AQUA
JF - Journal of Water Supply: Research and Technology - AQUA
IS - 7
ER -