CN115532235A - Lanthanum-based adsorbent and preparation method and application thereof - Google Patents
Lanthanum-based adsorbent and preparation method and application thereof Download PDFInfo
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- 239000003463 adsorbent Substances 0.000 title claims abstract description 72
- 229910052746 lanthanum Inorganic materials 0.000 title claims abstract description 67
- FZLIPJUXYLNCLC-UHFFFAOYSA-N lanthanum atom Chemical compound [La] FZLIPJUXYLNCLC-UHFFFAOYSA-N 0.000 title claims abstract description 67
- 238000002360 preparation method Methods 0.000 title claims abstract description 8
- 150000002603 lanthanum Chemical class 0.000 claims abstract description 26
- RHXSYTACTOMVLJ-UHFFFAOYSA-N 1H-benzimidazole-2-carboxylic acid Chemical class C1=CC=C2NC(C(=O)O)=NC2=C1 RHXSYTACTOMVLJ-UHFFFAOYSA-N 0.000 claims abstract description 17
- 229910019142 PO4 Inorganic materials 0.000 claims abstract description 11
- FDFPDGIMPRFRJP-UHFFFAOYSA-K trichlorolanthanum;heptahydrate Chemical compound O.O.O.O.O.O.O.[Cl-].[Cl-].[Cl-].[La+3] FDFPDGIMPRFRJP-UHFFFAOYSA-K 0.000 claims abstract description 9
- YXEUGTSPQFTXTR-UHFFFAOYSA-K lanthanum(3+);trihydroxide Chemical compound [OH-].[OH-].[OH-].[La+3] YXEUGTSPQFTXTR-UHFFFAOYSA-K 0.000 claims abstract description 7
- GJKFIJKSBFYMQK-UHFFFAOYSA-N lanthanum(3+);trinitrate;hexahydrate Chemical compound O.O.O.O.O.O.[La+3].[O-][N+]([O-])=O.[O-][N+]([O-])=O.[O-][N+]([O-])=O GJKFIJKSBFYMQK-UHFFFAOYSA-N 0.000 claims abstract description 6
- DJHGAFSJWGLOIV-UHFFFAOYSA-K Arsenate3- Chemical compound [O-][As]([O-])([O-])=O DJHGAFSJWGLOIV-UHFFFAOYSA-K 0.000 claims abstract description 3
- IGBVGUDGCXLPHR-UHFFFAOYSA-N C1=CC=C2N(CC(O)=O)C(C)N(CC(O)=O)C2=C1 Chemical group C1=CC=C2N(CC(O)=O)C(C)N(CC(O)=O)C2=C1 IGBVGUDGCXLPHR-UHFFFAOYSA-N 0.000 claims description 27
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 claims description 20
- 239000002904 solvent Substances 0.000 claims description 13
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 claims description 12
- 238000006243 chemical reaction Methods 0.000 claims description 9
- ICAKDTKJOYSXGC-UHFFFAOYSA-K lanthanum(iii) chloride Chemical compound Cl[La](Cl)Cl ICAKDTKJOYSXGC-UHFFFAOYSA-K 0.000 claims description 9
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 9
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- 238000000034 method Methods 0.000 claims description 7
- 150000004715 keto acids Chemical class 0.000 claims description 6
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- 150000002500 ions Chemical class 0.000 claims description 4
- 239000012266 salt solution Substances 0.000 claims description 4
- 238000001035 drying Methods 0.000 claims description 3
- 238000010438 heat treatment Methods 0.000 claims description 3
- 229910001385 heavy metal Inorganic materials 0.000 claims description 3
- 239000002594 sorbent Substances 0.000 claims 5
- 235000021317 phosphate Nutrition 0.000 claims 2
- 150000003013 phosphoric acid derivatives Chemical class 0.000 claims 2
- GCPXMJHSNVMWNM-UHFFFAOYSA-N arsenous acid Chemical class O[As](O)O GCPXMJHSNVMWNM-UHFFFAOYSA-N 0.000 claims 1
- 238000004519 manufacturing process Methods 0.000 claims 1
- 150000002823 nitrates Chemical class 0.000 claims 1
- 150000003467 sulfuric acid derivatives Chemical class 0.000 claims 1
- 238000001179 sorption measurement Methods 0.000 abstract description 48
- 239000011259 mixed solution Substances 0.000 abstract description 19
- 239000010452 phosphate Substances 0.000 abstract description 9
- NBIIXXVUZAFLBC-UHFFFAOYSA-K phosphate Chemical compound [O-]P([O-])([O-])=O NBIIXXVUZAFLBC-UHFFFAOYSA-K 0.000 abstract description 8
- 229940000489 arsenate Drugs 0.000 abstract description 3
- AQLMHYSWFMLWBS-UHFFFAOYSA-N arsenite(1-) Chemical compound O[As](O)[O-] AQLMHYSWFMLWBS-UHFFFAOYSA-N 0.000 abstract description 3
- 239000003344 environmental pollutant Substances 0.000 description 25
- 231100000719 pollutant Toxicity 0.000 description 25
- -1 oxo-acid radicals Chemical class 0.000 description 23
- 229910052751 metal Inorganic materials 0.000 description 17
- 239000002184 metal Substances 0.000 description 16
- 239000000203 mixture Substances 0.000 description 10
- 239000000243 solution Substances 0.000 description 10
- LDZYRENCLPUXAX-UHFFFAOYSA-N 2-methyl-1h-benzimidazole Chemical compound C1=CC=C2NC(C)=NC2=C1 LDZYRENCLPUXAX-UHFFFAOYSA-N 0.000 description 8
- 239000000463 material Substances 0.000 description 7
- 239000013110 organic ligand Substances 0.000 description 6
- 239000010865 sewage Substances 0.000 description 6
- 150000001450 anions Chemical class 0.000 description 5
- 238000002474 experimental method Methods 0.000 description 5
- 238000005516 engineering process Methods 0.000 description 4
- STZCRXQWRGQSJD-GEEYTBSJSA-M methyl orange Chemical compound [Na+].C1=CC(N(C)C)=CC=C1\N=N\C1=CC=C(S([O-])(=O)=O)C=C1 STZCRXQWRGQSJD-GEEYTBSJSA-M 0.000 description 4
- 229940012189 methyl orange Drugs 0.000 description 4
- 150000003254 radicals Chemical class 0.000 description 4
- 238000005660 chlorination reaction Methods 0.000 description 3
- 238000011109 contamination Methods 0.000 description 3
- RAXXELZNTBOGNW-UHFFFAOYSA-N imidazole Natural products C1=CNC=N1 RAXXELZNTBOGNW-UHFFFAOYSA-N 0.000 description 3
- 239000001048 orange dye Substances 0.000 description 3
- 229910002651 NO3 Inorganic materials 0.000 description 2
- QAOWNCQODCNURD-UHFFFAOYSA-L Sulfate Chemical compound [O-]S([O-])(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-L 0.000 description 2
- 239000002253 acid Substances 0.000 description 2
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 229910021645 metal ion Inorganic materials 0.000 description 2
- 239000002135 nanosheet Substances 0.000 description 2
- 239000001301 oxygen Substances 0.000 description 2
- 229910052760 oxygen Inorganic materials 0.000 description 2
- 239000000843 powder Substances 0.000 description 2
- 239000013535 sea water Substances 0.000 description 2
- 239000007787 solid Substances 0.000 description 2
- HYZJCKYKOHLVJF-UHFFFAOYSA-N 1H-benzimidazole Chemical compound C1=CC=C2NC=NC2=C1 HYZJCKYKOHLVJF-UHFFFAOYSA-N 0.000 description 1
- 239000002028 Biomass Substances 0.000 description 1
- 206010007269 Carcinogenicity Diseases 0.000 description 1
- 206010028980 Neoplasm Diseases 0.000 description 1
- 206010060860 Neurological symptom Diseases 0.000 description 1
- NHNBFGGVMKEFGY-UHFFFAOYSA-N Nitrate Chemical compound [O-][N+]([O-])=O NHNBFGGVMKEFGY-UHFFFAOYSA-N 0.000 description 1
- 229910052770 Uranium Inorganic materials 0.000 description 1
- XSQUKJJJFZCRTK-UHFFFAOYSA-N Urea Chemical compound NC(N)=O XSQUKJJJFZCRTK-UHFFFAOYSA-N 0.000 description 1
- TXTQARDVRPFFHL-UHFFFAOYSA-N [Sb].[H][H] Chemical compound [Sb].[H][H] TXTQARDVRPFFHL-UHFFFAOYSA-N 0.000 description 1
- 238000010521 absorption reaction Methods 0.000 description 1
- 229910052787 antimony Inorganic materials 0.000 description 1
- WATWJIUSRGPENY-UHFFFAOYSA-N antimony atom Chemical compound [Sb] WATWJIUSRGPENY-UHFFFAOYSA-N 0.000 description 1
- 239000007864 aqueous solution Substances 0.000 description 1
- LULLIKNODDLMDQ-UHFFFAOYSA-N arsenic(3+) Chemical compound [As+3] LULLIKNODDLMDQ-UHFFFAOYSA-N 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 201000011510 cancer Diseases 0.000 description 1
- 239000004202 carbamide Substances 0.000 description 1
- 230000007670 carcinogenicity Effects 0.000 description 1
- 231100000260 carcinogenicity Toxicity 0.000 description 1
- 239000013310 covalent-organic framework Substances 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- RYCXCWMKVIFLTC-UHFFFAOYSA-K dihydrogen phosphate;lanthanum(3+);carbonate Chemical compound [La+3].[O-]C([O-])=O.OP(O)([O-])=O RYCXCWMKVIFLTC-UHFFFAOYSA-K 0.000 description 1
- 239000003651 drinking water Substances 0.000 description 1
- 235000020188 drinking water Nutrition 0.000 description 1
- 230000005802 health problem Effects 0.000 description 1
- 231100000086 high toxicity Toxicity 0.000 description 1
- 238000001027 hydrothermal synthesis Methods 0.000 description 1
- 230000002452 interceptive effect Effects 0.000 description 1
- 238000004255 ion exchange chromatography Methods 0.000 description 1
- FYDKNKUEBJQCCN-UHFFFAOYSA-N lanthanum(3+);trinitrate Chemical compound [La+3].[O-][N+]([O-])=O.[O-][N+]([O-])=O.[O-][N+]([O-])=O FYDKNKUEBJQCCN-UHFFFAOYSA-N 0.000 description 1
- 239000003446 ligand Substances 0.000 description 1
- 239000008204 material by function Substances 0.000 description 1
- 239000012528 membrane Substances 0.000 description 1
- 229910044991 metal oxide Inorganic materials 0.000 description 1
- 150000004706 metal oxides Chemical class 0.000 description 1
- 239000012621 metal-organic framework Substances 0.000 description 1
- 230000004660 morphological change Effects 0.000 description 1
- 125000002524 organometallic group Chemical group 0.000 description 1
- 238000004064 recycling Methods 0.000 description 1
- 230000008929 regeneration Effects 0.000 description 1
- 238000011069 regeneration method Methods 0.000 description 1
- 206010040882 skin lesion Diseases 0.000 description 1
- 231100000444 skin lesion Toxicity 0.000 description 1
- NLJMYIDDQXHKNR-UHFFFAOYSA-K sodium citrate Chemical compound O.O.[Na+].[Na+].[Na+].[O-]C(=O)CC(O)(CC([O-])=O)C([O-])=O NLJMYIDDQXHKNR-UHFFFAOYSA-K 0.000 description 1
- 239000001509 sodium citrate Substances 0.000 description 1
- 238000004729 solvothermal method Methods 0.000 description 1
- JFALSRSLKYAFGM-UHFFFAOYSA-N uranium(0) Chemical compound [U] JFALSRSLKYAFGM-UHFFFAOYSA-N 0.000 description 1
- 125000005289 uranyl group Chemical group 0.000 description 1
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- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J20/00—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
- B01J20/22—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising organic material
- B01J20/223—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising organic material containing metals, e.g. organo-metallic compounds, coordination complexes
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/28—Treatment of water, waste water, or sewage by sorption
- C02F1/285—Treatment of water, waste water, or sewage by sorption using synthetic organic sorbents
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2101/00—Nature of the contaminant
- C02F2101/10—Inorganic compounds
- C02F2101/20—Heavy metals or heavy metal compounds
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Abstract
本发明公开了一种镧基吸附剂及其制备方法和应用,一种镧基吸附剂,为苯并咪唑羧酸衍生物和镧盐形成的配合物,所述镧盐包括七水合氯化镧、六水合硝酸镧和氢氧化镧。本发明制得的镧基吸附剂对锑酸根(Sb(V))、磷酸根(P(V))、亚砷酸根(As(III))、砷酸根(As(V))和亚锑酸根(Sb(III))的最大吸附量分别为896.5mg/g、426.9mg/g、271.7mg/g、154.6mg/g和91.5mg/g;在15min时,La‑MGs对Sb(V)、P(V)、As(III)、As(V)和Sb(III)的去除速率分别为97.8%、97.0%、87.3%、79.3%和80.4%;Sb(V)在吸附剂表面上的位点利用率达到50.1%,具有较高的位点利用率。此外,在混合溶液中,La‑MGs对Sb(V)具有较好的选择性能。The invention discloses a lanthanum-based adsorbent and its preparation method and application. The lanthanum-based adsorbent is a complex formed by a benzimidazole carboxylic acid derivative and a lanthanum salt. The lanthanum salt includes lanthanum chloride heptahydrate , Lanthanum nitrate hexahydrate and lanthanum hydroxide. The lanthanum-based adsorbent prepared by the present invention is effective against antimonate (Sb(V)), phosphate (P(V)), arsenite (As(III)), arsenate (As(V)) and antimonite The maximum adsorption capacity of (Sb(III)) was 896.5mg/g, 426.9mg/g, 271.7mg/g, 154.6mg/g and 91.5mg/g; The removal rates of P(V), As(III), As(V) and Sb(III) were 97.8%, 97.0%, 87.3%, 79.3% and 80.4%, respectively; the position of Sb(V) on the adsorbent surface The point utilization rate reaches 50.1%, which has a relatively high point utilization rate. In addition, in the mixed solution, La‑MGs has a good selectivity for Sb(V).
Description
技术领域technical field
本发明涉及重金属吸附剂领域,特别是一种镧基吸附剂及其制备方法和应用。The invention relates to the field of heavy metal adsorbents, in particular to a lanthanum-based adsorbent and its preparation method and application.
背景技术Background technique
水溶液中的含氧酸根污染,尤其是亚砷酸根(As(III))和锑(Sb(III))污染,由于其高毒性和致癌性,即使在低浓度下也对人类健康构成了巨大威胁,这已引起全球关注。饮用水被认为是砷(III)和锑(III)等含氧酸根污染的主要途径,这可能会导致严重的健康问题,如皮肤损伤、神经症状甚至癌症,这一特点要求采取有效的去除方法。吸附技术被认为是一种高效、简便的技术,与其他技术相比,它的效率更高。然而,由于吸附剂和不同污染物之间的匹配程度不同,导致靶向去除溶液中的特定污染物很困难。Oxygenate contamination in aqueous solutions, especially arsenite (As(III)) and antimony (Sb(III)) contamination, poses a great threat to human health even at low concentrations due to their high toxicity and carcinogenicity , which has attracted worldwide attention. Drinking water is considered to be a major route of contamination with oxo-acid radicals such as arsenic(III) and antimony(III), which can cause serious health problems such as skin lesions, neurological symptoms and even cancer, a feature that calls for effective removal methods . Adsorption technology is considered to be an efficient and simple technology, and its efficiency is higher compared to other technologies. However, targeted removal of specific pollutants in solution is difficult due to the varying degrees of matching between adsorbents and different pollutants.
近年来,人们致力于设计和构建合理的吸附结构,以提高对目标污染物的吸附性能。先进的功能材料如金属氧化物、金属-有机骨架、生物质基材料和共价有机骨架,都被用于探索吸附构型和污染物去除性能之间的关系。研究发现,具有较高晶格缺陷的UiO-66-SH-A由于形成了稳定的吸附构型,对As(III)/As(V)的吸附容量较大,速率较快。此外,MOFUiO-66-3C4N在模拟海水和天然海水中均表现出强大的铀酰吸附能力,这主要是由于较小的纳米袋增加了吸附剂与铀之间的配位作用。到目前为止,探索匹配程度对污染物在吸附剂上吸附性能的影响仍然是一个巨大的挑战,很少有人进行研究。In recent years, efforts have been made to design and construct rational adsorption structures to improve the adsorption performance for target pollutants. Advanced functional materials, such as metal oxides, metal-organic frameworks, biomass-based materials, and covalent organic frameworks, have been used to explore the relationship between adsorption configuration and pollutant removal performance. The study found that UiO-66-SH-A with higher lattice defects has a larger adsorption capacity and faster rate for As(III)/As(V) due to the formation of a stable adsorption configuration. In addition, MOFUiO-66-3C4N exhibited strong uranyl adsorption capacity in both simulated seawater and natural seawater, mainly due to the increased coordination between the adsorbent and uranium due to the smaller nanopockets. So far, exploring the effect of matching degree on the adsorption performance of pollutants on adsorbents is still a great challenge and few studies have been carried out.
公开号为CN113019305B的中国专利公开了多孔碱式碳酸镧磷酸盐吸附剂的制备及其应用。其中所述制备包括:将氯化镧、尿素及柠檬酸钠的混合溶液在120~180℃下进行水热反应,得到所述吸附剂。该发明的吸附剂对磷酸盐具有较快的吸附速率、较高的吸附容量和选择性,同时具有良好的再生和循环利用性。The Chinese patent with publication number CN113019305B discloses the preparation and application of porous basic lanthanum carbonate phosphate adsorbent. The preparation includes: subjecting a mixed solution of lanthanum chloride, urea and sodium citrate to a hydrothermal reaction at 120-180° C. to obtain the adsorbent. The adsorbent of the invention has faster adsorption rate, higher adsorption capacity and selectivity for phosphate, and has good regeneration and recycling properties.
公开号为CN103240060A的中国专利设计合成了新型的金属有机凝胶,是由苯并咪唑羧酸衍生物和金属铅离子形成配合物而束缚住溶剂小分子形成的凝胶。经SEM结果表明,该金属有机凝胶呈现交织的三维网状结构。对甲基橙染料分子的吸附实验表明,该金属有机凝胶可以在水相中高效选择性吸附甲基橙分子,因此,是一种处理甲基橙染料分子污染水的新型材料。The Chinese patent with the publication number CN103240060A designed and synthesized a new type of organometallic gel, which is a gel formed by forming complexes between benzimidazole carboxylic acid derivatives and metal lead ions to bind small solvent molecules. The results of SEM showed that the metal-organic gel presents an interwoven three-dimensional network structure. The adsorption experiments on methyl orange dye molecules show that the metal organic gel can efficiently and selectively adsorb methyl orange molecules in the water phase, so it is a new material for treating water polluted by methyl orange dye molecules.
公开号为CN113019305B的中国专利利用氯化镧制得吸附剂,对磷酸盐具有较快的吸附速率,公开号为CN103240060A的中国专利利用苯并咪唑羧酸衍生物制得金属有机凝胶,用于处理甲基橙染料分子污染水。目前尚没有技术将氯化镧、苯并咪唑羧酸衍生物应用于去除水中的含氧酸根离子污染。The Chinese patent whose publication number is CN113019305B utilizes lanthanum chloride to make an adsorbent, which has a faster adsorption rate for phosphate. Disposal of methyl orange dye molecule polluting water. At present, there is no technology to apply lanthanum chloride and benzimidazole carboxylic acid derivatives to remove oxoacid ion pollution in water.
发明内容Contents of the invention
本发明所要解决的技术问题是,针对现有技术不足,提供一种镧基吸附剂及其制备方法,能够高效、快速地捕获污水中的锑酸根,同时污水中的磷酸根对锑酸根去除影响较小。The technical problem to be solved by the present invention is to provide a lanthanum-based adsorbent and a preparation method thereof, which can efficiently and quickly capture antimonate in sewage, and at the same time, the phosphate in sewage has an influence on the removal of antimonate smaller.
本发明还提供了一种镧基吸附剂从含氧酸根中靶向去除锑酸根的应用。The invention also provides the application of a lanthanum-based adsorbent for targeted removal of antimonate radicals from oxoacid radicals.
为解决上述技术问题,本发明所采用的技术方案是:一种镧基吸附剂,为苯并咪唑羧酸衍生物和镧盐形成的配合物,所述镧盐包括七水合氯化镧、六水合硝酸镧和氢氧化镧。In order to solve the above-mentioned technical problems, the technical solution adopted in the present invention is: a lanthanum-based adsorbent, which is a complex formed by a benzimidazole carboxylic acid derivative and a lanthanum salt, and the lanthanum salt includes heptahydrate lanthanum chloride, hexahydrate Hydrated lanthanum nitrate and lanthanum hydroxide.
本发明合成镧基吸附剂因与不同污染物之间匹配程度不同,导致吸附剂与污染物之间配位作用力存在差异,从而影响材料的吸附性能。本发明相对于现有技术而言,本发明合成的镧基吸附剂能够高效、快速地捕获含氧酸根,尤其是锑酸根,同时发现混合溶液中磷酸根对锑酸根去除影响较小。因此,镧基吸附剂是一种处理含氧酸根污染水的新型材料。Due to the different matching degrees between the synthesized lanthanum-based adsorbent of the present invention and different pollutants, the coordination force between the adsorbent and the pollutants is different, thereby affecting the adsorption performance of the material. Compared with the prior art, the lanthanum-based adsorbent synthesized by the present invention can efficiently and rapidly capture oxoacids, especially antimonate, and it is found that the phosphate in the mixed solution has little effect on the removal of antimonate. Therefore, lanthanum-based adsorbent is a new type of material for treating water polluted by oxoacid radicals.
在本发明的一个优选的实施例中,所述苯并咪唑羧酸衍生物为1,3-二羧甲基-2-甲基苯并咪唑(MG),所述镧盐为七水合氯化镧。In a preferred embodiment of the present invention, the benzimidazole carboxylic acid derivative is 1,3-dicarboxymethyl-2-methylbenzimidazole (MG), and the lanthanum salt is heptahydrate chloride lanthanum.
实验中发现1,3-二羧甲基-2-甲基苯并咪唑(MG)和镧盐形成的镧基吸附剂La-MGs对Sb(V)的吸附性能优于2-甲基苯并咪唑(MC)和镧盐形成的镧基吸附剂La-MCs。所述的以1,3-二羧甲基-2-甲基苯并咪唑(MG)为有机配体所合成的镧基吸附剂具有多孔结构能够高效、快速和选择性地捕获混合溶液中的锑酸根,从而实现废水中含氧酸根的选择去除。形成的镧基吸附剂La-MGs中,当阴离子为氯化镧时,对Sb(V)的吸附性能依次优于阴离子为六水合硝酸镧和氢氧化镧的镧基吸附剂。In the experiment, it was found that the lanthanum-based adsorbent La-MGs formed by 1,3-dicarboxymethyl-2-methylbenzimidazole (MG) and lanthanum salt had better adsorption performance on Sb(V) than 2-methylbenzo Lanthanum-based adsorbent La-MCs formed by imidazole (MC) and lanthanum salt. The lanthanum-based adsorbent synthesized with 1,3-dicarboxymethyl-2-methylbenzimidazole (MG) as an organic ligand has a porous structure that can efficiently, rapidly and selectively capture the Antimonate, so as to realize the selective removal of oxo-acid in wastewater. In the formed lanthanum-based adsorbent La-MGs, when the anion is lanthanum chloride, the adsorption performance for Sb(V) is better than that of lanthanum-based adsorbents whose anions are lanthanum nitrate hexahydrate and lanthanum hydroxide.
在本发明的一个优选的实施例中,所述苯并咪唑羧酸衍生物与所述氯化镧的摩尔比为1.25~5mmol:2.5~10mmol。进一步优选地,所述苯并咪唑羧酸衍生物与所述氯化镧的摩尔比为1.25~5mmol:2.5~5mmol。In a preferred embodiment of the present invention, the molar ratio of the benzimidazole carboxylic acid derivative to the lanthanum chloride is 1.25-5 mmol: 2.5-10 mmol. Further preferably, the molar ratio of the benzimidazole carboxylic acid derivative to the lanthanum chloride is 1.25-5 mmol: 2.5-5 mmol.
本发明还公开了一种镧基吸附剂的制备方法,包括以下步骤:The invention also discloses a preparation method of a lanthanum-based adsorbent, comprising the following steps:
S1、将镧盐溶于溶剂中,形成镧盐溶液;S1, dissolving the lanthanum salt in a solvent to form a lanthanum salt solution;
S2、在S1的镧盐溶液中加入苯并咪唑羧酸衍生物混合均匀后,加热烘干,反应结束后,得到镧基吸附剂。S2. Add benzimidazole carboxylic acid derivatives to the lanthanum salt solution of S1, mix evenly, heat and dry, and obtain a lanthanum-based adsorbent after the reaction is completed.
在本发明的一个优选的实施例中,S2中加热烘干的温度为120℃~180℃,时间为8~24h。时间和温度不同都会对材料吸附性能不同,目前所选择的温度和时间是使材料获得最大吸附量的。所形成的形貌结构为纳米片堆积的多孔结构,而吸附不同污染物后形貌发生了明显的变化。In a preferred embodiment of the present invention, the temperature of heating and drying in S2 is 120° C. to 180° C., and the time is 8 to 24 hours. Different time and temperature will have different adsorption properties of the material. The currently selected temperature and time are to make the material obtain the maximum adsorption capacity. The formed morphology structure is a porous structure with nanosheets stacked, and the morphology changes significantly after adsorbing different pollutants.
在本发明的一个优选的实施例中,所述苯并咪唑羧酸衍生物为1,3-二羧甲基-2-甲基苯并咪唑(MG),所述镧盐为七水合氯化镧。In a preferred embodiment of the present invention, the benzimidazole carboxylic acid derivative is 1,3-dicarboxymethyl-2-methylbenzimidazole (MG), and the lanthanum salt is heptahydrate chloride lanthanum.
在本发明的一个优选的实施例中,所述苯并咪唑羧酸衍生物与所述镧盐的摩尔比为1.25~5mmol:2.5~10mmol。In a preferred embodiment of the present invention, the molar ratio of the benzimidazole carboxylic acid derivative to the lanthanum salt is 1.25-5 mmol: 2.5-10 mmol.
在本发明的一个优选的实施例中,S1中溶剂为水、甲醇和无水乙醇;优选地,S1中溶剂为无水乙醇。In a preferred embodiment of the present invention, the solvent in S1 is water, methanol and absolute ethanol; preferably, the solvent in S1 is absolute ethanol.
所述苯并咪唑羧酸衍生物、所述镧盐、无水乙醇的摩尔体积比为1.25~5mmol:2.5~10mmol:30-60mL。The molar volume ratio of the benzimidazole carboxylic acid derivative, the lanthanum salt, and absolute ethanol is 1.25˜5 mmol: 2.5˜10 mmol: 30-60 mL.
S2中混合的方式为超声混匀30~60min。The mixing method in S2 is ultrasonic mixing for 30-60 minutes.
本发明还公开了一种利用所述的镧基吸附剂靶向去除污水中的含氧酸根的应用。The invention also discloses an application of using the lanthanum-based adsorbent for targeted removal of oxygen-containing acid radicals in sewage.
在本发明的一个优选的实施例中,所述污水中包括含氧酸根和其它重金属离子,所述含氧酸根包括锑酸根(Sb(V))、磷酸根(P(V))、亚砷酸根(As(III))、砷酸根(As(V))和亚锑酸根(Sb(III)),且靶向去除所述含氧酸根的过程中,不受污水中的磷酸根、硝酸根、硫酸根的影响;优选地,靶向去除的含氧酸根为锑酸根(Sb(V))。In a preferred embodiment of the present invention, the sewage includes oxoacids and other heavy metal ions, and the oxoacids include antimonate (Sb(V)), phosphate (P(V)), arsenous acid radical (As(III)), arsenate radical (As(V)) and antimonite radical (Sb(III)), and in the process of targeted removal of said oxoacid radicals, phosphate radicals and nitrate radicals in sewage are not affected , the impact of sulfate; preferably, the oxoacid for targeted removal is antimonate (Sb(V)).
与现有技术相比,本发明所具有的有益效果为:本发明通过改变污染物与吸附剂的匹配程度,调控污染物与吸附位点的配位作用力,从而影响污染物在吸附材料表面的去除性能。本发明制得的镧基吸附剂对锑酸根(Sb(V))、磷酸根(P(V))、亚砷酸根(As(III))、砷酸根(As(V))和亚锑酸根(Sb(III))的最大吸附量分别为896.5mg/g、426.9mg/g、271.7mg/g、154.6mg/g和91.5mg/g;在15min时,La-MGs对Sb(V)、P(V)、As(III)、As(V)和Sb(III)的去除速率分别为97.8%、97.0%、87.3%、79.3%和80.4%;Sb(V)在吸附剂表面上的位点利用率达到50.1%,具有较高的位点利用率。此外,在混合溶液中,La-MGs对Sb(V)具有较好的选择性能。该工作从去除对象的角度探讨吸附位点的局部配位环境对吸附性能的影响,为污染物的选择性高效的吸附提供一种新的思路。Compared with the prior art, the beneficial effects of the present invention are as follows: the present invention regulates the coordination force between the pollutant and the adsorption site by changing the matching degree of the pollutant and the adsorbent, thereby affecting the adsorption of the pollutant on the surface of the adsorption material. removal performance. The lanthanum-based adsorbent prepared by the present invention is effective against antimonate (Sb(V)), phosphate (P(V)), arsenite (As(III)), arsenate (As(V)) and antimonite The maximum adsorption capacity of (Sb(III)) was 896.5mg/g, 426.9mg/g, 271.7mg/g, 154.6mg/g and 91.5mg/g respectively; The removal rates of P(V), As(III), As(V) and Sb(III) were 97.8%, 97.0%, 87.3%, 79.3% and 80.4%, respectively; the position of Sb(V) on the adsorbent surface The point utilization rate reaches 50.1%, which has a relatively high point utilization rate. In addition, La-MGs have good selectivity for Sb(V) in the mixed solution. This work explores the influence of the local coordination environment of the adsorption site on the adsorption performance from the perspective of removal objects, and provides a new idea for the selective and efficient adsorption of pollutants.
附图说明Description of drawings
图1两种配体的镧基吸附剂对Sb(V)的吸附性能;The lanthanum-based adsorbent of two kinds of ligands is to the adsorption performance of Sb(V) of Fig. 1;
图2三种不同阴离子的镧基吸附剂对Sb(V)的吸附性能;Figure 2 The adsorption properties of three different anion-based lanthanum-based adsorbents for Sb(V);
图3三种不同溶剂中得到的镧基吸附剂对Sb(V)的吸附性能;The adsorption properties of lanthanum-based adsorbents obtained in three different solvents to Sb(V) in Fig. 3;
图4金属离子与有机配体比例得到的镧基吸附剂对Sb(V)的吸附性能;The adsorption performance of the lanthanum-based adsorbent obtained by the ratio of metal ions and organic ligands to Sb(V) in Fig. 4;
图5镧基吸附剂捕获不同污染物前后的形貌变化;Figure 5. Morphological changes before and after capturing different pollutants by lanthanum-based adsorbents;
图6Sb(V)在镧基吸附剂的吸附性能;Figure 6Sb(V) adsorption performance on lanthanum-based adsorbent;
图7P(V)在镧基吸附剂的吸附性能;Figure 7P (V) adsorption performance on lanthanum-based adsorbent;
图8As(III)在镧基吸附剂的吸附性能;The adsorption performance of Fig. 8As(III) on lanthanum-based adsorbent;
图9As(V)在镧基吸附剂的吸附性能;Figure 9As (V) in the adsorption performance of lanthanum-based adsorbent;
图10Sb(III)在镧基吸附剂的吸附性能;Figure 10Sb(III) adsorption performance on lanthanum-based adsorbent;
图11低浓度下La-MGs的选择性实验。CSb(V)=2mM,V=50mL,吸附剂剂量=1.0g/L,pH=3,t=24h,T=25℃。Figure 11 Selectivity experiment of La-MGs at low concentration. C Sb(V) = 2 mM, V = 50 mL, adsorbent dose = 1.0 g/L, pH = 3, t = 24 h, T = 25 °C.
具体实施方式detailed description
实施例1Example 1
本实施例中的所述镧基吸附剂是以1,3-二羧甲基-2-甲基苯并咪唑为有机配体,七水合氯化镧为金属中心,以水、甲醇和无水乙醇为溶剂,采用溶剂热法制备的。The lanthanum-based adsorbent in this example uses 1,3-dicarboxymethyl-2-methylbenzimidazole as the organic ligand, lanthanum chloride heptahydrate as the metal center, and water, methanol and anhydrous Ethanol is used as solvent and prepared by solvothermal method.
(1)将金属盐七水合氯化镧、1,3-二羧甲基-2-甲基苯并咪唑与无水乙醇混合,超声混匀30min后得到混合溶液;其中金属盐七水合氯化镧、1,3-二羧甲基-2-甲基苯并咪唑与无水乙醇的摩尔体积比为8mmol:4mmol:40mL。(1) Mix the metal salt heptahydrate lanthanum chloride, 1,3-dicarboxymethyl-2-methylbenzimidazole and absolute ethanol, and obtain a mixed solution after ultrasonic mixing for 30 minutes; the metal salt heptahydrate chlorination The molar volume ratio of lanthanum, 1,3-dicarboxymethyl-2-methylbenzimidazole and absolute ethanol is 8mmol:4mmol:40mL.
(2)将所述步骤(1)得到的混合溶液置于烘箱中反应,反应的温度为120℃,时间为12h,得到镧基吸附剂La-MGs。(2) Put the mixed solution obtained in the step (1) into an oven for reaction at a temperature of 120° C. for 12 hours to obtain the lanthanum-based adsorbent La-MGs.
实施例2Example 2
(1)将金属盐七水合氯化镧、2-甲基苯并咪唑(MC)与无水乙醇混合,超声混匀30min后得到混合溶液;其中金属盐七水合氯化镧、2-甲基苯并咪唑(MC)与无水乙醇的摩尔体积比为8mmol:4mmol:40mL。(1) Mix the metal salt lanthanum chloride heptahydrate, 2-methylbenzimidazole (MC) and absolute ethanol, and obtain a mixed solution after ultrasonic mixing for 30 minutes; wherein the metal salt lanthanum chloride heptahydrate, 2-methyl The molar volume ratio of benzimidazole (MC) to absolute ethanol is 8mmol:4mmol:40mL.
(2)将所述步骤(1)得到的混合溶液置于烘箱中反应,反应的温度为120℃,时间为12h,得到镧基吸附剂La-MCs。(2) Put the mixed solution obtained in the step (1) into an oven for reaction at a temperature of 120° C. for 12 hours to obtain the lanthanum-based adsorbent La-MCs.
由有机配体2-甲基苯并咪唑(MC)和1,3-二羧甲基-2-甲基苯并咪唑(MG)分别和金属盐七水合氯化镧制备镧基吸附剂。如图1所示,实验中发现1,3-二羧甲基-2-甲基苯并咪唑(MG)和镧盐形成的镧基吸附剂La-MGs对Sb(V)的吸附性能优于2-甲基苯并咪唑(MC)和镧盐形成的镧基吸附剂La-MCs。以1,3-二羧甲基-2-甲基苯并咪唑(MG)为有机配体所合成的镧基吸附剂具有多孔结构能够高效、快速和选择性地捕获混合溶液中的锑酸根,从而实现废水中含氧酸根的选择去除。Lanthanum-based adsorbents were prepared from organic ligands 2-methylbenzimidazole (MC) and 1,3-dicarboxymethyl-2-methylbenzimidazole (MG) and metal salt lanthanum chloride heptahydrate, respectively. As shown in Figure 1, it was found in the experiment that the lanthanum-based adsorbent La-MGs formed by 1,3-dicarboxymethyl-2-methylbenzimidazole (MG) and lanthanum salt has better adsorption performance on Sb(V) than Lanthanum-based adsorbent La-MCs formed by 2-methylbenzimidazole (MC) and lanthanum salt. The lanthanum-based adsorbent synthesized with 1,3-dicarboxymethyl-2-methylbenzimidazole (MG) as an organic ligand has a porous structure that can efficiently, quickly and selectively capture antimonate in mixed solutions, In this way, the selective removal of oxygen-containing acid radicals in wastewater can be realized.
实施例3Example 3
(1)将镧盐、1,3-二羧甲基-2-甲基苯并咪唑与无水乙醇混合,超声混匀45min后得到混合溶液;其中镧盐、1,3-二羧甲基-2-甲基苯并咪唑与无水乙醇的摩尔体积比为8mmol:4mmol:40mL。其中镧盐分别为七水合氯化镧、六水合硝酸镧和氢氧化镧。(1) Mix lanthanum salt, 1,3-dicarboxymethyl-2-methylbenzimidazole and absolute ethanol, and obtain a mixed solution after ultrasonic mixing for 45 minutes; among them, lanthanum salt, 1,3-dicarboxymethyl -The molar volume ratio of 2-methylbenzimidazole to absolute ethanol is 8mmol:4mmol:40mL. Wherein the lanthanum salts are lanthanum chloride heptahydrate, lanthanum nitrate hexahydrate and lanthanum hydroxide respectively.
(2)将所述步骤(1)得到的混合溶液置于烘箱中反应,反应的温度为120℃,时间为12h,分别制得阴离子为氯化镧、六水合硝酸镧、氢氧化镧的白色粉末固体LaCl3-MGs、淡黄色粉末固体La(NO3)3-MGs和白色块状估计La(OH)3-MGs。(2) The mixed solution obtained in the step (1) is placed in an oven to react, the temperature of the reaction is 120° C., and the time is 12 hours, and the anions are respectively lanthanum chloride, lanthanum nitrate hexahydrate, and lanthanum hydroxide. Powder solid LaCl 3 -MGs, light yellow powder solid La(NO 3 ) 3 -MGs and white block estimated La(OH) 3 -MGs.
如图2所示形成的镧基吸附剂La-MGs中,阴离子为氯化镧对Sb(V)的吸附性能依次优于六水合硝酸镧和氢氧化镧。In the lanthanum-based adsorbent La-MGs formed as shown in Figure 2, the adsorption performance of Sb(V) with lanthanum chloride as an anion is sequentially better than that of lanthanum nitrate hexahydrate and lanthanum hydroxide.
实施例4Example 4
(1)将金属盐七水合氯化镧、1,3-二羧甲基-2-甲基苯并咪唑与溶剂混合,超声混匀30min后得到混合溶液;其中金属盐七水合氯化镧、1,3-二羧甲基-2-甲基苯并咪唑与溶剂的摩尔体积比为8mmol:4mmol:40ml。其中溶剂分别选用为水、甲醇和无水乙醇。(1) Mix the metal salt lanthanum chloride heptahydrate, 1,3-dicarboxymethyl-2-methylbenzimidazole with the solvent, and ultrasonically mix for 30 minutes to obtain a mixed solution; wherein the metal salt lanthanum chloride heptahydrate, The molar volume ratio of 1,3-dicarboxymethyl-2-methylbenzimidazole to solvent is 8mmol:4mmol:40ml. Wherein the solvent is selected as water, methanol and absolute ethanol respectively.
(2)将所述步骤(1)得到的混合溶液置于烘箱中反应,反应的温度为120℃,时间为12h,得到镧基吸附剂La-MGs。(2) Put the mixed solution obtained in the step (1) into an oven for reaction at a temperature of 120° C. for 12 hours to obtain the lanthanum-based adsorbent La-MGs.
如图3所示,三种不同溶剂中得到的镧基吸附剂对Sb(V)的吸附性能中无水乙醇制得的镧基吸附剂La-MGs对Sb(V)的吸附性能最佳。As shown in Figure 3, the adsorption performance of lanthanum-based adsorbents obtained in three different solvents on Sb(V) was the best among the lanthanum-based adsorbents prepared from absolute ethanol, La-MGs, for Sb(V).
实施例5Example 5
(1)将金属盐七水合氯化镧、1,3-二羧甲基-2-甲基苯并咪唑与无水乙醇混合,超声混匀30min后得到混合溶液;无水乙醇的体积为40mL,金属盐七水合氯化镧、1,3-二羧甲基-2-甲基苯并咪唑的比例分别为0.5:1、1:1、2:1。(1) Mix metal salt lanthanum chloride heptahydrate, 1,3-dicarboxymethyl-2-methylbenzimidazole and absolute ethanol, and ultrasonically mix for 30 minutes to obtain a mixed solution; the volume of absolute ethanol is 40mL , the ratios of metal salt lanthanum chloride heptahydrate and 1,3-dicarboxymethyl-2-methylbenzimidazole are 0.5:1, 1:1, and 2:1, respectively.
(2)将所述步骤(1)得到的混合溶液置于烘箱中反应,反应的温度为120℃,时间为12h,得到镧基吸附剂La-MGs。(2) Put the mixed solution obtained in the step (1) into an oven for reaction at a temperature of 120° C. for 12 hours to obtain the lanthanum-based adsorbent La-MGs.
图4为金属离子与有机配体比例得到的镧基吸附剂对Sb(V)的吸附性能,当金属盐七水合氯化镧、1,3-二羧甲基-2-甲基苯并咪唑的比例为2:1时,得到的镧基吸附剂对Sb(V)的吸附性能最佳。因此金属盐七水合氯化镧、1,3-二羧甲基-2-甲基苯并咪唑较优的比例区间为1:1~2:1。Figure 4 shows the adsorption properties of lanthanum-based adsorbents obtained by the ratio of metal ions to organic ligands to Sb(V). When the ratio of 2:1, the obtained lanthanum-based adsorbent has the best adsorption performance for Sb(V). Therefore, the optimal ratio range of metal salt lanthanum chloride heptahydrate and 1,3-dicarboxymethyl-2-methylbenzimidazole is 1:1-2:1.
实施例6Example 6
(1)将金属盐七水合氯化镧、1,3-二羧甲基-2-甲基苯并咪唑与无水乙醇混合,超声混匀30min后得到混合溶液;其中金属盐七水合氯化镧、1,3-二羧甲基-2-甲基苯并咪唑与无水乙醇的摩尔体积比为8mmol:4mmol:40mL。(1) Mix the metal salt heptahydrate lanthanum chloride, 1,3-dicarboxymethyl-2-methylbenzimidazole and absolute ethanol, and obtain a mixed solution after ultrasonic mixing for 30 minutes; the metal salt heptahydrate chlorination The molar volume ratio of lanthanum, 1,3-dicarboxymethyl-2-methylbenzimidazole and absolute ethanol is 8mmol:4mmol:40mL.
(2)将所述步骤(1)得到的混合溶液置于烘箱中反应,反应的温度为120℃,时间为8h,得到镧基吸附剂La-MGs。(2) Put the mixed solution obtained in the step (1) into an oven for reaction at a temperature of 120° C. for 8 hours to obtain the lanthanum-based adsorbent La-MGs.
实施例7Example 7
(1)将金属盐七水合氯化镧、1,3-二羧甲基-2-甲基苯并咪唑与无水乙醇混合,超声混匀30min后得到混合溶液;其中金属盐七水合氯化镧、1,3-二羧甲基-2-甲基苯并咪唑与无水乙醇的摩尔体积比为8mmol:4mmol:40mL。(1) Mix the metal salt heptahydrate lanthanum chloride, 1,3-dicarboxymethyl-2-methylbenzimidazole and absolute ethanol, and obtain a mixed solution after ultrasonic mixing for 30 minutes; the metal salt heptahydrate chlorination The molar volume ratio of lanthanum, 1,3-dicarboxymethyl-2-methylbenzimidazole and absolute ethanol is 8mmol:4mmol:40mL.
(2)将所述步骤(1)得到的混合溶液置于烘箱中反应,反应的温度为180℃,时间为24h,得到镧基吸附剂La-MGs。(2) Put the mixed solution obtained in the step (1) into an oven for reaction at a temperature of 180° C. for 24 hours to obtain the lanthanum-based adsorbent La-MGs.
将实施例1中得到的镧基吸附剂加入到初始浓度为1g/L(五种污染的初始浓度)五种污染物溶液反应24h,然后测试溶液中物种污染物的残余浓度,得到镧基吸附剂对五种污染物(Sb(V)、P(V)、As(III)、As(V)和Sb(III))的吸附量依次为896.5mg/g、426.9mg/g、271.7mg/g、154.6mg/g和91.5mg/g,如图6-10所示。图5为镧基吸附剂捕获不同污染物前后的形貌变化,所形成的形貌结构为纳米片堆积的多孔结构,而吸附不同污染物后形貌发生了明显的变化。Adding the lanthanum-based adsorbent obtained in Example 1 to an initial concentration of 1g/L (initial concentrations of five pollutions) five kinds of pollutant solutions reacted for 24h, then tested the residual concentration of species pollutants in the solution to obtain lanthanum-based adsorption The adsorption amounts of the five pollutants (Sb(V), P(V), As(III), As(V) and Sb(III)) were 896.5mg/g, 426.9mg/g, 271.7mg/g g, 154.6mg/g and 91.5mg/g, as shown in Figure 6-10. Figure 5 shows the morphology changes of the lanthanum-based adsorbent before and after capturing different pollutants. The formed morphology structure is a porous structure with nanosheets stacked, and the morphology changes significantly after adsorbing different pollutants.
应用例1Application example 1
配制初始浓度为2mM Sb(V)溶液,通过在实验溶液中加入预定量的F-,NO3 -,H2PO4 -,AsO2 -,SbO2 -、SO4 2-和AsO4 2-来检测干扰离子的对Sb(V)吸附性能的影响,取50mL于锥形瓶中,在锥形瓶中分别加入50mg实施例1中制备的镧基吸附剂,在25℃、180r/min条件下,放入恒温震荡箱中,反应24h,取出锥形瓶,通过0.45um滤膜过滤备用。溶液中残留的As浓度用ICP检测、残留的Sb浓度用原子吸收光谱仪检测、残留的P(V)、F-、NO3 -、Cl-和SO4 2-浓度用离子色谱检测。Prepare an initial concentration of 2mM Sb(V) solution by adding a predetermined amount of F - , NO 3 - , H 2 PO 4 - , AsO 2 - , SbO 2 - , SO 4 2- and AsO 4 2- To detect the influence of interfering ions on the adsorption performance of Sb (V), get 50mL in the Erlenmeyer flask, add 50mg of the lanthanum-based adsorbent prepared in Example 1 respectively in the Erlenmeyer flask, at 25 ° C, 180r/min conditions , put it into a constant temperature shaking box, react for 24 hours, take out the Erlenmeyer flask, and filter through a 0.45um filter membrane for later use. The concentration of residual As in the solution was detected by ICP, the concentration of residual Sb was detected by atomic absorption spectrometer, and the concentration of residual P(V), F - , NO 3 - , Cl - and SO 4 2- was detected by ion chromatography.
Sb(V)、P(V)、As(III)、As(V)、Sb(III)、F-、NO3 -、Cl-和SO4 2-的吸附容量(Qe)的计算遵循如下公式:The calculation of the adsorption capacity (Q e ) of Sb(V), P(V), As(III), As(V), Sb(III), F - , NO 3 - , Cl - and SO 4 2- follows the following formula:
式中:C0为初始溶液中不同污染物的浓度(mg/L);Ce为吸附后溶液中不同污染物的浓度(mg/L);Qe为镧基吸附剂对不同污染物的浓度的吸附容量(mg/g);V为锥形瓶中吸附对象溶液的体积(mL);m为投加镧基吸附剂的质量(mg)。In the formula: C 0 is the concentration of different pollutants in the initial solution (mg/L); C e is the concentration of different pollutants in the solution after adsorption (mg/L); Q e is the concentration of different pollutants in the lanthanum-based adsorbent The adsorption capacity of the concentration (mg/g); V is the volume of the solution to be adsorbed in the Erlenmeyer flask (mL); m is the mass of the lanthanum-based adsorbent added (mg).
根据上述公式,可计算出不同污染物在溶液浓度为2mM时镧基吸附剂对的吸附性能,具体结果见图11。靶向去除锑酸根(Sb(V))的过程中,不受污水中的磷酸根、硝酸根、硫酸根的影响。选择实验表明镧基吸附剂对Sb(V)具有不错的选择性,能够从八种污染物中选择性捕获Sb(V)。不同污染物吸附在La-MGs上的位点利用率如表1所示,其中Sb(V)的吸附位点的利用率为50.1%。According to the above formula, the adsorption performance of the lanthanum-based adsorbent pair for different pollutants can be calculated when the solution concentration is 2 mM, and the specific results are shown in Figure 11. During the targeted removal of antimonate (Sb(V)), it is not affected by phosphate, nitrate, and sulfate in sewage. Selection experiments show that the lanthanum-based adsorbent has good selectivity to Sb(V), and can selectively capture Sb(V) from eight pollutants. The site utilization ratios of different pollutants adsorbed on La-MGs are shown in Table 1, among which the utilization ratio of Sb(V) adsorption sites was 50.1%.
表1.不同污染物吸附在La-MGs上的位点利用率Table 1. Site utilization of different pollutants adsorbed on La-MGs
a:La-MGs吸附剂中吸附位点的总量是8mM。a: The total amount of adsorption sites in La-MGs adsorbent is 8 mM.
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