可氧化再生的“核-壳”结构磁性吸附剂Mn0.6Zn0.4Fe2O4@SiO2-CeO2对水中氧氟沙星的吸附机制
doi: 10.13801/j.cnki.fhclxb.20210722.002
Adsorption mechanism of ofloxacin in water with "core-shell" magnetic adsorbent Mn0.6Zn0.4Fe2O4@SiO2-CeO2 capable of oxidation regeneration
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摘要: 为去除水中难生物降解的氧氟沙星(OFLX),突破吸附剂固液分离和再生难的瓶颈,采用SiO2和CeO2功能化修饰Mn0.6Zn0.4Fe2O4磁性纳米颗粒,制备得到磁性纳米复合物吸附剂Mn0.6Zn0.4Fe2O4@SiO2-CeO2,利用XRD、FTIR、SEM、TEM、和振动样品磁强计等对Mn0.6Zn0.4Fe2O4@SiO2-CeO2进行了系统表征。3种动力学模型(拟一级动力学、拟二级动力学和颗粒内扩散模型)、3种等温线模型(Langmuir、Freundlich和D-R模型)和吸附热力学的研究结果表明:该吸附过程的速率由颗粒内扩散和液膜扩散等多种因素共同控制;该吸附过程以物理吸附为主,化学吸附为吸附速率控制步骤;吸附过程可自发进行,为放热和熵减小的过程。FTIR和XRD的表征结果表明,π-π共轭作用、分子间氢键和配位作用等是Mn0.6Zn0.4Fe2O4@SiO2-CeO2和OFLX之间的主要相互作用力。经6次吸附-氧化原位再生循环后,Mn0.6Zn0.4Fe2O4@SiO2-CeO2对OFLX平衡吸附量为27.00 mg·g−1。研究结果可为难生物降解的OFLX的控制技术研究提供基础理论数据。Abstract: In order to remove ofloxacin (OFXL), which is difficult to biodegrade in water, and break through the bottleneck of solid-liquid separation and regeneration of adsorbents, Mn0.6Zn0.4Fe2O4 magnetic nanoparticles were modified by SiO2 and CeO2 to prepare Mn0.6Zn0.4Fe2O4@SiO2-CeO2 magnetic nanocompsite adsorbents. The as-prepared Mn0.6Zn0.4Fe2O4@SiO2-CeO2 were systematically characterized using XRD, FTIR, SEM, TEM, vibration sample magnetometer. The investigation results of three kinetic models (quasi-first-order kinetics, quasi-second-order kinetics, and intraparticle diffusion models), three isotherm models (Langmuir, Freundlich and D-R models) and adsorption thermodynamics show that the adsorption rate is controlled by multiple factors such as intra-particle diffusion and liquid film diffusion; the adsorption process is dominated by physical adsorption, and the chemical adsorption is the rate-controlling step; the adsorption process is spontaneously and exothermic with entropy increase. The characterization results of FTIR and XRD spectroscopy indicate that the interaction forces between Mn0.6Zn0.4Fe2O4@SiO2-CeO2 and OFLX include π-π conjugation, hydrogen bonding and coordination. After six cycles of adsorption-oxidation regeneration in situ, the equilibrium adsorption capacity of Mn0.6Zn0.4Fe2O4@SiO2-CeO2 for OFLX is 27.00 mg·g−1. The research results can provide basic theoretical data on the control technology of nonbiodegradable OFLX.
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Key words:
- magnetic adsorbent /
- CeO2 /
- oxidation regeneration /
- ofloxacin /
- adsorption mechanism /
- "core-shell" structure
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表 1 Mn0.6Zn0.4Fe2O4@SiO2-CeO2吸附OFLX的吸附动力学拟合结果
Table 1. Fitting results of adsorption kinetics of OFLX by Mn0.6Zn0.4Fe2O4@SiO2-CeO2
Temperature/K qe,exp/ (mg·g−1) Quasi-first-order kinetic model Quasi-second-order kinetic model qe,cal/(mg·g−1) K1/min−1 R2 qe,cal/(mg·g−1) K2/min−1 R2 298 25.17 23.54 −0.2419 0.9691 24.74 0.01784 0.9943 308 23.72 22.24 −0.2638 0.9712 23.29 0.02166 0.9946 318 26.49 25.15 −0.2702 0.9792 26.26 0.02039 0.9976 Notes: qe,exp—Experimental amount of OFLX removed per unit mass of adsorbent; K1, K2—Quasi-first-order kinetic constant and quasi-second-order kinetic constant; qe,cal—Calculation amount of OFLX removed per unit mass of adsorbent. 表 2 Mn0.6Zn0.4Fe2O4@SiO2-CeO2吸附OFLX的吸附等温线模型的拟合结果
Table 2. Fitting results of adsorption isotherms models of OFLX by Mn0.6Zn0.4Fe2O4@SiO2-CeO2
Temperature/K Langmuir Freundlich qm/(mg·g−1) b/(L·mg−1) R2 Kf/(mg·g−1) n/(mg·g−1) R2 298 33.98 0.7189 0.9651 16.81 4.430 0.9899 308 35.47 0.3340 0.9944 13.72 3.650 0.9941 318 46.01 0.3322 0.9961 16.51 3.226 0.9735 Notes: qm—Langmuir adsorption maximum; b—Langmuir coefficient of distribution of the adsorption; Kf—Freundlich coefficient of distribution of the adsorption; n—Freundlich isotherm constant. 表 3 Mn0.6Zn0.4Fe2O4@SiO2-CeO2的D-R等温吸附模型的拟合结果
Table 3. Fitting results of D-R isotherm adsorption model of Mn0.6Zn0.4Fe2O4@SiO2-CeO2
Temperature/K qm/(mg·g−1) k/10−7(mol2·kJ−2) E/(kJ·mol−1) R2 298 41.89 0.462 3.29 0.8089 308 62.43 0.102 7.00 0.9280 318 87.18 1.050 2.18 0.9973 Notes: qm—D-R adsorption maximum; k—Adsorption energy constant; E—Free energy of adsorption. 表 4 Mn0.6Zn0.4Fe2O4@SiO2-CeO2吸附OFLX的热力学参数
Table 4. Thermodynamic parameters of adsorption of OFLX by Mn0.6Zn0.4Fe2O4@SiO2-CeO2
Temperature/K lnKd ΔGΘ/(kJ·mol−1) ΔHΘ/(kJ·mol−1) ΔSΘ/(J·mol−1·K−1) 298 4.817 −11.93 −43.8 −107.83 308 3.675 −9.41 318 3.411 −9.02 Notes: Kd—Adsorption thermodynamic equilibrium constant; ΔGΘ—Gibbs free energy variation of the adsorption process; ΔHΘ—Enthalpy change of the adsorption process; ΔSΘ—Entropy change of theadsorption process. 表 5 不同吸附材料对OFLX吸附性能比较
Table 5. Comparison of the adsorption performance of OFLX by different adsorption materials
Adsorption material BET/(m2·g−1) Balance time/min qe/(mg·g−1) Reference Magnetic biochar 254 1440 22.00 [32] Zrconium-based MOFs 519 120 35.46 [33] Shell polysacchar/biochar composites 141 1300 6.64 [34] MCM41 1026 120 39.20 [35] Mn0.6Zn0.4Fe2O4@SiO2-CeO2 169 120 30.38 This report Notes: BET—Specific surface area; MOFs—Metal organic framework; MCM41—Ordered mesoporous molecular sieve. -
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