Recent development and application of mixed metal oxides in wastewater treatment: A review
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摘要: 混合金属氧化物(Mixed metal oxide,MMO),即一种以上金属的氧化物,因其在水中结构的独特变化,能展现出较强的吸附性能和催化活性,在废水处理方面具有极大应用潜力。本文综述了MMO的制备方法,主要可分为固相烧结法、聚合物前驱体焙烧法、层状双金属氢氧化物(Layered double hydroxides,LDHs)前驱体焙烧法、化学共沉淀法和水热法5种,并详细介绍了通过改变这些合成方法与合成条件实现的MMO元素组成、元素比例、形貌结构等的控制,以调控其性质性能。系统分析了MMO在去除重金属、类金属、有机污染物和阴离子方面的主要机制及研究进展,其中主要机制为在MMO结构重组过程中,伴随有吸附、催化及其协同作用。得益于这3种机制MMO不仅能实现单一污染物的高效脱除,还能实现多污染物的同步去除,在废水处理方面有着显著成效,但目前大多数研究仍停留在实验阶段,在实际废水处理及工程应用上的研究尚少。
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关键词:
- 混合金属氧化物(MMO) /
- 废水处理 /
- 重金属 /
- 有机污染物 /
- 阴离子
Abstract: Mixed metal oxides (MMO) containing more than one type of metal, have shown great application potential to be adsorbents and catalysts due to their unique structural changes in water. Therefore, they have great potential in wastewater treatment. In this paper, the preparation methods of MMO are described, including solid-phase sintering, polymeric precursor calcination, layered double hydroxides precursor calcination, chemical coprecipitation and hydrothermal methods, and control methods of the element composition, element proportion, and structure of MMO to regulate their properties by changing these synthesis methods and conditions are introduced in detail. The main mechanisms of MMO in the removal of heavy metals, metalloids, organic pollutants and anionic are comprehensively analyzed which can be summarized as: in the process of structural reorganization of MMO, adsorption, catalysis and their synergy are accompanied. MMO can not only remove single pollutants efficiently, but also remove multiple pollutants simultaneously due to these three effects, so MMO have significant effects in effluent treatment, but at present most of the research is still at the experimental stage, and there are few studies on effluent treatment and engineering applications.-
Key words:
- mixed metal oxide /
- wastewater treatment /
- heavy metals /
- organic pollutants /
- anionic
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表 1 混合金属氧化物(MMO)的不同制备方法及条件
Table 1. Different preparation methods and conditions of mixed metal oxide (MMO)
Synthetic method MMO Raw material pH Other conditions Calcination temperature/℃ Preparation time/h Ref. Solid-phase sintering CaAl-MMO CaO, Al2O3 — — 1200 4-5 [15] Polymer precursor calcination method ZnAlNiZr-MMO Zn(NO3)2·6H2O, Al(NO3)3·9H2O, Ni(NO3)2·6H2O, Zr(NO3)4·5H2O, C6H8O7·H2O, HOCH2CH2OH — Stir at 60-70℃, stir at 80-
90℃ and heat treat at 300℃550 18-24 [16] CoCu-MMO Co(NO3)2·6H2O, Cu(NO3)2·3H2O, C6H8O7·H2O, CH3CH2OH — Stir at normal atmospheric temperature and heat to 80℃ 500 53-55 [17] LDHs precursor calcination method MgAl-MMO Mg(NO3)2·6H2O, Al(NO3)3·9H2O, NaOH, Na2CO3 9.0 Refluxing crystallization 500 13-15 [18] CoCr-MMO Co(NO3)2·6H2O, Cr(NO3)3·9H2O, NaOH, Na2CO3 9.0 Age at 80℃ for 24 h, stir,
60℃ drying400 40-42 [19] Chemical coprecipitation FeSn-MMO Na2SnO3, FeCl3, NaOH 5.3 Stir, precipitate, 70℃ drying 250 11-13 [20] FeZr-MMO Zr(SO4)2·4H2O, FeSO4·7H2O, NaOH 7.5 Stir, precipitate, aging,
65℃ drying— — [21] Hydrothermal method SbMo-MMO SbCl3, NaMoO6·2H2O, CH3CH2OH — Magnetic stir, pressure cooker 180℃ for 24 h — >24 [22] Note: LDHs—Layered double hydroxides. 表 2 MMO处理水中污染物的应用
Table 2. Application of MMO in the wastewater treatment
Contaminant MMO Application Adsorption
capacity/(mg·g−1)Removal
efficiency/%Mechanism Ref. Heavy metal ZnSn-MMO Cu2+, Pb2+, Zn2+ 38.9, 117.2, 29.1 — Surface complexation and adsorption [50] FeMn-MMO Pb2+ 108.1 — Surface complexation and adsorption [51] MgAl-MMO Cd2+, Pb2+ 386.1, 359.7 — Surface complexation and adsorption [52] FeZr-MMO Cr(Ⅵ) 59.9 — Reorganization and surface adsorption [53] MgAl-MMO Cr(Ⅵ) 94.6 — Reorganization and surface adsorption [54] Metalloid FeZr-MMO Se(IV) 277.0 — Reorganization and surface adsorption [55] MgAl2O4 Se(IV) 179.6 — Reorganization and surface adsorption [49] FeZr-MMO Sb(V) 51.0 — Reorganization and surface adsorption [21] FeMn-MMO Sb(V) 95.0 — Reorganization and surface adsorption [37] FeMn-MMO As(V) 132.8 — Reorganization and surface adsorption [56] FeAl-MMO As(III) 314.9 >99.0 Catalysis and adsorption [57] CuFe-MMO As(III) 118.1 — Catalysis and adsorption [58] Organic pollutants FeMn-MMO TCE — 100 Catalysis [59] NiCo2O4 AP — 99.5 Catalysis [60] CoNi-MMO PR — 70.0 Adsorption [61] FeMn-MMO RBK5 — 88.0 Catalysis [62] 1D ZnO-ZnFe2O4 CR 263.0 — Adsorption [13] Nd-CoAl-MMO AR — 100 Catalysis [63]
Halogen ionMgAl-MMO Br–, I– 362.3 — Reorganization and surface adsorption [47] MgZr-MMO F– 144.1 — Reorganization and surface adsorption [64] LaZr-MMO F– — 97.0 Reorganization and surface adsorption [65] CaAl-MMO Cl– 105.9, 96.0 — Reorganization and surface adsorption [15] Oxyanion ZnAl−MMO SO42– 62.5 — Reorganization and surface adsorption [66] CeAl-MMO PO43– 70.4 — Reorganization and surface adsorption [67] CeAl-MMO PO43– 249.3 — Reorganization and surface adsorption [68] Other anions MgAl-MMO S2– — 82.0 Reorganization and surface adsorption [69] Notes: TCE—Trichloroethylene; AP—4−acetaminophenol; PR—Procion red; RBK5—Reactive black 5; CR—Congo red; AR14—Acid red 14. -
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