CIESC Journal ›› 2025, Vol. 76 ›› Issue (10): 5290-5299.DOI: 10.11949/0438-1157.20250356
• Energy and environmental engineering • Previous Articles Next Articles
Shuang HAN(
), Qiuyue WANG, Ze-Xian LOW(
), Zhaoxiang ZHONG, Weihong XING(
)
Received:2025-04-08
Revised:2025-05-31
Online:2025-11-25
Published:2025-10-25
Contact:
Ze-Xian LOW, Weihong XING
通讯作者:
刘泽贤,邢卫红
作者简介:韩霜(2001—),女,硕士研究生,hans@njtech.edu.cn
CLC Number:
Shuang HAN, Qiuyue WANG, Ze-Xian LOW, Zhaoxiang ZHONG, Weihong XING. Fabrication of PVDF/LFTCO (LaFe0.55Ti0.2Co0.25O3) catalytic membrane for photo-Fenton-like degradation of tetracycline hydrochloride[J]. CIESC Journal, 2025, 76(10): 5290-5299.
韩霜, 王秋月, 刘泽贤, 仲兆祥, 邢卫红. PVDF/LFTCO(LaFe0.55Ti0.2Co0.25O3)催化膜类光芬顿降解盐酸四环素[J]. 化工学报, 2025, 76(10): 5290-5299.
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Fig.3 SEM image (a) and EDX mapping (b) of LFTCO-0.2; SEM images of PVDF (c) and PVDF/LFTCO catalytic membranes with 2, 5, and 10 mg catalysts loads [(d)—(f)]
| 项目 | 检测结果 |
|---|---|
| 孔径 | 0.22 μm |
| 厚度 | 100~120 μm |
| 直径 | (50.00±0.30) mm |
| 水流速 | 8.22 ml/(cm2·min) |
| 泡点 | 300 MPa |
Table 1 Product information of PVDF commercial membranes
| 项目 | 检测结果 |
|---|---|
| 孔径 | 0.22 μm |
| 厚度 | 100~120 μm |
| 直径 | (50.00±0.30) mm |
| 水流速 | 8.22 ml/(cm2·min) |
| 泡点 | 300 MPa |
Fig.6 The degradation of PVDF/LFTCO membranes in different reaction systems [Experiment conditions: initial pollutant concentration 10 mg/L, catalyst load 5 mg, H2O2 concentration 20 mmol/L, membrane flux 334.39 L/(m2·h), light intensity 100 mW/cm2, natural pH except for the specific varied parameter]
Fig.7 Effects of catalyst load (a), H2O2 concentration (b) and feed flow rate (c) on TCH degradation [Experiment conditions: initial pollutant concentration 10 mg/L, catalyst load 5 mg, H2O2 concentration 20 mmol/L, membrane flux 334.39 L/(m2·h), light intensity 100 mW/cm2, natural pH except for the specific varied parameter]
| 催化剂 | 污染物 | 催化类型 | 通量/(L/(m2·h)) | 去除效果/% | 文献 |
|---|---|---|---|---|---|
| S,N双掺杂碳(SNC) | 四环素 | 过氧一硫酸盐 | 1726.65 | 91 | [ |
| Fe@NC | 2,4-二氯苯酚 | 过氧一硫酸盐 | 306 | 99.2 | [ |
| Cu-MOF-74 | 四环素 | 过氧一硫酸盐 | 274.6 | 69.8 | [ |
| CuFeS2 | 莫西沙星 | 过氧一硫酸盐 | 344.8 | 68.2 | [ |
| ZCO | 磷酸氯喹 | 过氧一硫酸盐 | 192 | 45.3 | [ |
| ZnIn2S4 | 盐酸四环素 | 光催化 | 84.06 | 90 | [ |
| Co@CNT-GO | 阿特拉津 | 过氧一硫酸盐 | 95.3 | 79 | [ |
| LFTCO | 盐酸四环素 | 光芬顿 | 334.39 | 87.78 | 本工作 |
Table 2 Comparison of organic contaminant degradation performance by PVDF vacuum filtration-supported catalytic membranes of previous researches
| 催化剂 | 污染物 | 催化类型 | 通量/(L/(m2·h)) | 去除效果/% | 文献 |
|---|---|---|---|---|---|
| S,N双掺杂碳(SNC) | 四环素 | 过氧一硫酸盐 | 1726.65 | 91 | [ |
| Fe@NC | 2,4-二氯苯酚 | 过氧一硫酸盐 | 306 | 99.2 | [ |
| Cu-MOF-74 | 四环素 | 过氧一硫酸盐 | 274.6 | 69.8 | [ |
| CuFeS2 | 莫西沙星 | 过氧一硫酸盐 | 344.8 | 68.2 | [ |
| ZCO | 磷酸氯喹 | 过氧一硫酸盐 | 192 | 45.3 | [ |
| ZnIn2S4 | 盐酸四环素 | 光催化 | 84.06 | 90 | [ |
| Co@CNT-GO | 阿特拉津 | 过氧一硫酸盐 | 95.3 | 79 | [ |
| LFTCO | 盐酸四环素 | 光芬顿 | 334.39 | 87.78 | 本工作 |
Fig.8 Catalytic degradation effect of TCH under different pH conditions [Experiment conditions: initial pollutant concentration 10 mg/L, catalyst load 5 mg, H2O2 concentration 20 mmol/L, membrane flux 334.39 L/(m2·h), light intensity 100 mW/cm2]
Fig.9 Cyclic catalytic degradation performance of PVDF/LFTCO membrane [Experiment conditions: initial pollutant concentration 10 mg/L, catalyst load 5 mg, H2O2 concentration 20 mmol/L, membrane flux 334.39 L/(m2·h), light intensity 100 mW/cm2]
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