生态环境学报 ›› 2026, Vol. 35 ›› Issue (2): 267-277.DOI: 10.16258/j.cnki.1674-5906.2026.02.010
范铭洋1,2(
), 郭春彬2,3, 邹晶晶1,2,*(
), 罗根华1,4, 刘越雌1, 徐颖1,2,*(
)
收稿日期:2025-07-29
修回日期:2026-01-13
接受日期:2026-01-26
出版日期:2026-02-18
发布日期:2026-02-09
通讯作者:
邹晶晶,徐颖
作者简介:范铭洋(2000年生),女(蒙古族),硕士研究生,研究方向为水环境污染治理研究。E-mail: 472321939@stu.lntu.edu.cn
基金资助:
FAN Mingyang1,2(
), GUO Chunbin2,3, ZOU Jingjing1,2,*(
), LUO Genhua1,4, LIU Yueci1, XU Ying1,2,*(
)
Received:2025-07-29
Revised:2026-01-13
Accepted:2026-01-26
Online:2026-02-18
Published:2026-02-09
摘要:
为了吸附工业废水中的磺胺嘧啶(SDZ),该研究旨在将固体废弃物煤气化渣(CGS)进行水热改性,制备出吸附性能良好的吸附剂——改性煤气化渣(HCGS),并分析和探索其物理化学特性、吸附性能及机理。通过对CGS进行不同酸浓度和温度条件下的改性处理,对不同改性条件下氧化物浸出量、硅羟基(Si−OH)含量和吸附性能的皮尔逊相关性进行分析,对吸附条件进行探究,结合XRD、FT-IR、SEM、BET、XPS等表征分析,结果表明,最佳改性温度为80 ℃、盐酸质量分数为16%;HCGS比表面积可达326 m2∙g−1、对SDZ的吸附量可达24.8 mg∙g−1;改性机制主要与硅羟基的生成和羟基质子化有关;最佳吸附时间为180 min,SDZ的初始质量浓度为20 mg∙L−1,pH为8,吸附剂投加量为30 mg;吸附过程符合准二级动力学模型,是以化学吸附为主的非均相扩散过程;颗粒内扩散模型表明吸附过程除内扩散之外还受到其他因素的影响;吸附机理与氢键和静电作用有关。该研究将CGS转化为高性能低成本的吸附材料,实现固废资源化与抗生素污染治理的双重目标,为抗生素工业废水治理提供了理论基础与技术支持。
中图分类号:
范铭洋, 郭春彬, 邹晶晶, 罗根华, 刘越雌, 徐颖. 改性煤气化渣对水中磺胺嘧啶吸附性能及机理研究[J]. 生态环境学报, 2026, 35(2): 267-277.
FAN Mingyang, GUO Chunbin, ZOU Jingjing, LUO Genhua, LIU Yueci, XU Ying. Study on the Adsorption Performance and Mechanism of Modified Coal Gasification Slag for Sulfadiazine in Aquatic Environment[J]. Ecology and Environmental Sciences, 2026, 35(2): 267-277.
| 组成 | SiO2 | Al2O3 | TiO2 | CaO | Fe2O3 | MgO | LOI |
|---|---|---|---|---|---|---|---|
| 质量分数/% | 42.5 | 21.4 | 2.2 | 6.2 | 11.4 | 3.9 | 12.4 |
表1 煤气化渣样品的化学成分
Table 1 Chemical compositions of the coal gasification slag sample
| 组成 | SiO2 | Al2O3 | TiO2 | CaO | Fe2O3 | MgO | LOI |
|---|---|---|---|---|---|---|---|
| 质量分数/% | 42.5 | 21.4 | 2.2 | 6.2 | 11.4 | 3.9 | 12.4 |
| 质量浓度/ (mg∙L−1) | 准一级动力学模型 | 准二级动力学模型 | Elovich 模型 | ||||||||
|---|---|---|---|---|---|---|---|---|---|---|---|
| k1/min−1 | q1e/(mg∙g−1) | r12 | k2/(g∙mg−1∙min−1) | q2e/(mg∙g−1) | r22 | β/(g∙mg−1) | α/(mg∙g−1∙min−1) | re2 | |||
| 20 | 0.012 | 5.9 | 0.961 | 0.013 | 24.9 | 0.999 | 0.655 | 4.81×103 | 0.961 | ||
表2 吸附SDZ的动力学模型拟合结果
Table 2 Kinetics model fitting results of adsorbed SDZ
| 质量浓度/ (mg∙L−1) | 准一级动力学模型 | 准二级动力学模型 | Elovich 模型 | ||||||||
|---|---|---|---|---|---|---|---|---|---|---|---|
| k1/min−1 | q1e/(mg∙g−1) | r12 | k2/(g∙mg−1∙min−1) | q2e/(mg∙g−1) | r22 | β/(g∙mg−1) | α/(mg∙g−1∙min−1) | re2 | |||
| 20 | 0.012 | 5.9 | 0.961 | 0.013 | 24.9 | 0.999 | 0.655 | 4.81×103 | 0.961 | ||
| 质量浓度/ (mg∙L−1) | 颗粒内扩散模型 | ||||||||
|---|---|---|---|---|---|---|---|---|---|
| kd1/(mg∙g−1∙min−0.5) | w1/(mg∙g−1) | rd12 | kd2/(mg∙g−1∙min−0.5) | w2/(mg∙g−1) | rd22 | kd3/(mg∙g−1∙min−0.5) | w3/(mg∙g−1) | rd32 | |
| 20 | 1.372 | 14.688 | 0.962 | 0.518 | 18.582 | 0.895 | 0.046 | 23.684 | 0.758 |
表3 吸附SDZ的颗粒内扩散模型拟合结果
Table 3 Intra-particle diffusion model fitting results of adsorbed SDZ
| 质量浓度/ (mg∙L−1) | 颗粒内扩散模型 | ||||||||
|---|---|---|---|---|---|---|---|---|---|
| kd1/(mg∙g−1∙min−0.5) | w1/(mg∙g−1) | rd12 | kd2/(mg∙g−1∙min−0.5) | w2/(mg∙g−1) | rd22 | kd3/(mg∙g−1∙min−0.5) | w3/(mg∙g−1) | rd32 | |
| 20 | 1.372 | 14.688 | 0.962 | 0.518 | 18.582 | 0.895 | 0.046 | 23.684 | 0.758 |
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