Journal of Synthetic Crystals ›› 2025, Vol. 54 ›› Issue (8): 1478-1490.DOI: 10.16553/j.cnki.issn1000-985x.2025.0037
• Research Articles • Previous Articles
SHI Weiye1(
), LIU Sihan1, ZHAO Shuchang2, WANG Shuai1, WANG Zhongbao1, HUO Chunqing1(
)
Received:2025-02-26
Online:2025-08-20
Published:2025-09-01
CLC Number:
SHI Weiye, LIU Sihan, ZHAO Shuchang, WANG Shuai, WANG Zhongbao, HUO Chunqing. Investigation on Performance and Mechanism of the Falling Film-Type Plasma-Fenton Synergistic System in Treatment of KN-R Wastewater[J]. Journal of Synthetic Crystals, 2025, 54(8): 1478-1490.
Fig.2 Schematic diagram of the falling film dielectric barrier discharge (DBD) plasma reactor for low-temperature plasma treatment (1 represents the inner electrode, 2 denotes the ground electrode, 3 signifies the quartz tube, and 4 indicates the water storage tank)
Fig.3 Influence of initial solution concentration on the degradation efficiency of reactive brilliant blue KN-R (a), and the fitting results of the first-order reaction kinetics (b)
Fig.5 Impact of discharge power on the degradation efficiency of reactive brilliant blue KN-R (a), and the first-order reaction kinetics fitting results (b)
| Current/A | Input power/W | Output power/W | Output efficiency/% |
|---|---|---|---|
| 1.70 | 136 | 61.93 | 45.54 |
| 1.80 | 144 | 73.50 | 51.04 |
| 1.90 | 152 | 79.66 | 52.40 |
| 2.00 | 160 | 83.34 | 52.09 |
Table 1 Calculations of input power, output power and energy output efficiency (input voltage 80 V)
| Current/A | Input power/W | Output power/W | Output efficiency/% |
|---|---|---|---|
| 1.70 | 136 | 61.93 | 45.54 |
| 1.80 | 144 | 73.50 | 51.04 |
| 1.90 | 152 | 79.66 | 52.40 |
| 2.00 | 160 | 83.34 | 52.09 |
Fig.6 Impact of initial pH on the degradation of reactive brilliant blue KN-R (a), the first-order reaction kinetics fitting results (b), and the variation in solution pH value during the treatment process (c)
Fig.8 Effects of Fe2+ addition on the degradation efficiency of reactive brilliant blue KN-R (a), a performance comparison with the single DBD system (b), and the variation in H2O2 concentration in the solution during the treatment process (c) in the DBD/Fenton system
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