CIESC Journal ›› 2023, Vol. 74 ›› Issue (5): 2217-2227.DOI: 10.11949/0438-1157.20230044
• Energy and environmental engineering • Previous Articles Next Articles
Quanbi ZHANG(), Yijin YANG(), Xujing GUO
Received:
2023-01-18
Revised:
2023-03-28
Online:
2023-06-29
Published:
2023-05-05
Contact:
Yijin YANG
通讯作者:
羊依金
作者简介:
张全碧(1998—),女,硕士研究生,zhangquanbi666@163.com
基金资助:
CLC Number:
Quanbi ZHANG, Yijin YANG, Xujing GUO. Catalytic degradation of dissolved organic matter in rifampicin pharmaceutical wastewater by Fenton oxidation process[J]. CIESC Journal, 2023, 74(5): 2217-2227.
张全碧, 羊依金, 郭旭晶. 芬顿氧化法对利福平制药废水中溶解性有机物的催化降解[J]. 化工学报, 2023, 74(5): 2217-2227.
名称 | 利福平/ (mg·L-1) | pH | CODCr/ (mg·L-1) | BOD5/ (mg·L-1) | SS/ (mg·L-1) | 色度 |
---|---|---|---|---|---|---|
利福平废水 | 10~20 | 6.8 | 90.02 | 21.55 | 7.63 | 10倍 |
Table 1 Water quality parameters
名称 | 利福平/ (mg·L-1) | pH | CODCr/ (mg·L-1) | BOD5/ (mg·L-1) | SS/ (mg·L-1) | 色度 |
---|---|---|---|---|---|---|
利福平废水 | 10~20 | 6.8 | 90.02 | 21.55 | 7.63 | 10倍 |
影响因素 | 实验设计 |
---|---|
反应时间/min | 10、20、30、60、120、180、240、300 |
pH | 1、2、3、4、5、6、7 |
硫酸亚铁浓度/(g·L-1) | 0.2、0.3、0.4、0.5、0.6 |
H2O2浓度/(ml·L-1) | 0.8、1.1、1.4、1.7、2.0 |
Table 2 Degradation experimental design
影响因素 | 实验设计 |
---|---|
反应时间/min | 10、20、30、60、120、180、240、300 |
pH | 1、2、3、4、5、6、7 |
硫酸亚铁浓度/(g·L-1) | 0.2、0.3、0.4、0.5、0.6 |
H2O2浓度/(ml·L-1) | 0.8、1.1、1.4、1.7、2.0 |
Fig.5 Synchronous map and asynchronous map (the white regions represent positive correlations, whereas the grey regions represent negative correlations)
相关系数 | Peak275 | Peak315 | Peak365 | Peak400 | Peak460 | Peak473 | Peak500 | Peak567 |
---|---|---|---|---|---|---|---|---|
R2 | 0.1967 | 0.4288 | 0.9084 | 0.9779 | 0.9111 | 0.8781 | 0.7801 | 0.5312 |
Table 3 Correlation between fluorescence intensity of each peak and COD
相关系数 | Peak275 | Peak315 | Peak365 | Peak400 | Peak460 | Peak473 | Peak500 | Peak567 |
---|---|---|---|---|---|---|---|---|
R2 | 0.1967 | 0.4288 | 0.9084 | 0.9779 | 0.9111 | 0.8781 | 0.7801 | 0.5312 |
各峰 | 1级 | 2级 | BMG | ||||
---|---|---|---|---|---|---|---|
k1/min-1 | R2 | k 2/(10-6min-1) | R2 | 1/b | 1/m | R2 | |
Peak275 | 0.0047 | 0.1265 | 6.8503 | 0.2509 | 0.9095 | 1.5805 | 0.9991 |
Peak315 | 0.0061 | 0.2880 | 2.5344 | 0.5008 | 0.9500 | 1.7687 | 0.9993 |
Peak365 | 0.0052 | 0.3974 | 2.0935 | 0.6367 | 0.8925 | 0.5964 | 0.9996 |
Peak400 | 0.0059 | 0.3954 | 1.6718 | 0.6847 | 0.9233 | 0.7703 | 0.9999 |
Peak460 | 0.0056 | 0.3576 | 1.5457 | 0.6429 | 0.9217 | 0.8450 | 0.9999 |
Peak473 | 0.0052 | 0.2348 | 2.7397 | 0.5437 | 0.9095 | 0.8013 | 0.9999 |
Peak500 | 0.0038 | 0.3283 | 0.8610 | 0.5207 | 0.8389 | 0.5456 | 0.9999 |
Peak567 | 0.0026 | 0.4143 | 0.7464 | 0.5401 | 0.6637 | 0.1770 | 0.9992 |
Table 4 The degradation kinetics of fluorescent substance
各峰 | 1级 | 2级 | BMG | ||||
---|---|---|---|---|---|---|---|
k1/min-1 | R2 | k 2/(10-6min-1) | R2 | 1/b | 1/m | R2 | |
Peak275 | 0.0047 | 0.1265 | 6.8503 | 0.2509 | 0.9095 | 1.5805 | 0.9991 |
Peak315 | 0.0061 | 0.2880 | 2.5344 | 0.5008 | 0.9500 | 1.7687 | 0.9993 |
Peak365 | 0.0052 | 0.3974 | 2.0935 | 0.6367 | 0.8925 | 0.5964 | 0.9996 |
Peak400 | 0.0059 | 0.3954 | 1.6718 | 0.6847 | 0.9233 | 0.7703 | 0.9999 |
Peak460 | 0.0056 | 0.3576 | 1.5457 | 0.6429 | 0.9217 | 0.8450 | 0.9999 |
Peak473 | 0.0052 | 0.2348 | 2.7397 | 0.5437 | 0.9095 | 0.8013 | 0.9999 |
Peak500 | 0.0038 | 0.3283 | 0.8610 | 0.5207 | 0.8389 | 0.5456 | 0.9999 |
Peak567 | 0.0026 | 0.4143 | 0.7464 | 0.5401 | 0.6637 | 0.1770 | 0.9992 |
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