CN114950352B - Lanthanum carbonate modified Fe 3 O 4 Dephosphorization adsorbent at@C and preparation method and application thereof - Google Patents
Lanthanum carbonate modified Fe 3 O 4 Dephosphorization adsorbent at@C and preparation method and application thereof Download PDFInfo
- Publication number
- CN114950352B CN114950352B CN202110213537.6A CN202110213537A CN114950352B CN 114950352 B CN114950352 B CN 114950352B CN 202110213537 A CN202110213537 A CN 202110213537A CN 114950352 B CN114950352 B CN 114950352B
- Authority
- CN
- China
- Prior art keywords
- lanthanum carbonate
- preparation
- lanthanum
- phosphorus removal
- modified
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Active
Links
- 239000003463 adsorbent Substances 0.000 title claims abstract description 50
- 229910017569 La2(CO3)3 Inorganic materials 0.000 title claims abstract description 31
- NZPIUJUFIFZSPW-UHFFFAOYSA-H lanthanum carbonate Chemical compound [La+3].[La+3].[O-]C([O-])=O.[O-]C([O-])=O.[O-]C([O-])=O NZPIUJUFIFZSPW-UHFFFAOYSA-H 0.000 title claims abstract description 31
- 229960001633 lanthanum carbonate Drugs 0.000 title claims abstract description 31
- 238000002360 preparation method Methods 0.000 title claims abstract description 22
- OAICVXFJPJFONN-UHFFFAOYSA-N Phosphorus Chemical compound [P] OAICVXFJPJFONN-UHFFFAOYSA-N 0.000 claims abstract description 31
- 229910052698 phosphorus Inorganic materials 0.000 claims abstract description 31
- 239000011574 phosphorus Substances 0.000 claims abstract description 31
- 229910052746 lanthanum Inorganic materials 0.000 claims abstract description 27
- FZLIPJUXYLNCLC-UHFFFAOYSA-N lanthanum atom Chemical compound [La] FZLIPJUXYLNCLC-UHFFFAOYSA-N 0.000 claims abstract description 24
- 229910019142 PO4 Inorganic materials 0.000 claims abstract description 21
- 239000000463 material Substances 0.000 claims abstract description 19
- NBIIXXVUZAFLBC-UHFFFAOYSA-K phosphate Chemical compound [O-]P([O-])([O-])=O NBIIXXVUZAFLBC-UHFFFAOYSA-K 0.000 claims abstract description 19
- 239000010452 phosphate Substances 0.000 claims abstract description 19
- 239000002105 nanoparticle Substances 0.000 claims abstract description 16
- 230000007935 neutral effect Effects 0.000 claims abstract description 13
- 230000002378 acidificating effect Effects 0.000 claims abstract description 7
- 238000001027 hydrothermal synthesis Methods 0.000 claims abstract description 7
- 238000000151 deposition Methods 0.000 claims abstract description 3
- 238000001556 precipitation Methods 0.000 claims abstract description 3
- 238000004729 solvothermal method Methods 0.000 claims abstract description 3
- XEEYBQQBJWHFJM-UHFFFAOYSA-N iron Substances [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 claims description 97
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 40
- 239000000243 solution Substances 0.000 claims description 31
- LYCAIKOWRPUZTN-UHFFFAOYSA-N Ethylene glycol Chemical compound OCCO LYCAIKOWRPUZTN-UHFFFAOYSA-N 0.000 claims description 30
- 238000006243 chemical reaction Methods 0.000 claims description 23
- 238000003756 stirring Methods 0.000 claims description 21
- 238000001035 drying Methods 0.000 claims description 17
- 238000000034 method Methods 0.000 claims description 16
- 150000002505 iron Chemical class 0.000 claims description 13
- WQZGKKKJIJFFOK-GASJEMHNSA-N Glucose Natural products OC[C@H]1OC(O)[C@H](O)[C@@H](O)[C@@H]1O WQZGKKKJIJFFOK-GASJEMHNSA-N 0.000 claims description 10
- 239000008103 glucose Substances 0.000 claims description 10
- 238000012546 transfer Methods 0.000 claims description 10
- 239000000725 suspension Substances 0.000 claims description 9
- VMHLLURERBWHNL-UHFFFAOYSA-M Sodium acetate Chemical compound [Na+].CC([O-])=O VMHLLURERBWHNL-UHFFFAOYSA-M 0.000 claims description 8
- 229940040526 anhydrous sodium acetate Drugs 0.000 claims description 8
- 150000002603 lanthanum Chemical class 0.000 claims description 8
- 239000002202 Polyethylene glycol Substances 0.000 claims description 7
- CZMRCDWAGMRECN-UGDNZRGBSA-N Sucrose Chemical compound O[C@H]1[C@H](O)[C@@H](CO)O[C@@]1(CO)O[C@@H]1[C@H](O)[C@@H](O)[C@H](O)[C@@H](CO)O1 CZMRCDWAGMRECN-UGDNZRGBSA-N 0.000 claims description 7
- 229930006000 Sucrose Natural products 0.000 claims description 7
- WQZGKKKJIJFFOK-VFUOTHLCSA-N beta-D-glucose Chemical compound OC[C@H]1O[C@@H](O)[C@H](O)[C@@H](O)[C@@H]1O WQZGKKKJIJFFOK-VFUOTHLCSA-N 0.000 claims description 7
- 229920001223 polyethylene glycol Polymers 0.000 claims description 7
- 239000005720 sucrose Substances 0.000 claims description 7
- 239000002904 solvent Substances 0.000 claims description 5
- 238000002604 ultrasonography Methods 0.000 claims description 5
- 229910052760 oxygen Inorganic materials 0.000 claims description 4
- BVKZGUZCCUSVTD-UHFFFAOYSA-M Bicarbonate Chemical compound OC([O-])=O BVKZGUZCCUSVTD-UHFFFAOYSA-M 0.000 claims description 3
- 239000007864 aqueous solution Substances 0.000 claims description 3
- BVKZGUZCCUSVTD-UHFFFAOYSA-N carbonic acid Chemical compound OC(O)=O BVKZGUZCCUSVTD-UHFFFAOYSA-N 0.000 claims description 3
- 229910002554 Fe(NO3)3·9H2O Inorganic materials 0.000 claims description 2
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 claims description 2
- 229910002422 La(NO3)3·6H2O Inorganic materials 0.000 claims description 2
- 229910052739 hydrogen Inorganic materials 0.000 claims description 2
- 239000001257 hydrogen Substances 0.000 claims description 2
- 229910052742 iron Inorganic materials 0.000 claims description 2
- 230000035484 reaction time Effects 0.000 claims description 2
- 239000012266 salt solution Substances 0.000 claims description 2
- QTBSBXVTEAMEQO-UHFFFAOYSA-N Acetic acid Chemical compound CC(O)=O QTBSBXVTEAMEQO-UHFFFAOYSA-N 0.000 claims 3
- DGAQECJNVWCQMB-PUAWFVPOSA-M Ilexoside XXIX Chemical compound C[C@@H]1CC[C@@]2(CC[C@@]3(C(=CC[C@H]4[C@]3(CC[C@@H]5[C@@]4(CC[C@@H](C5(C)C)OS(=O)(=O)[O-])C)C)[C@@H]2[C@]1(C)O)C)C(=O)O[C@H]6[C@@H]([C@H]([C@@H]([C@H](O6)CO)O)O)O.[Na+] DGAQECJNVWCQMB-PUAWFVPOSA-M 0.000 claims 1
- 239000011734 sodium Substances 0.000 claims 1
- 229910052708 sodium Inorganic materials 0.000 claims 1
- 238000001179 sorption measurement Methods 0.000 abstract description 63
- 239000002131 composite material Substances 0.000 abstract description 22
- 230000005389 magnetism Effects 0.000 abstract description 6
- 230000007613 environmental effect Effects 0.000 abstract description 5
- 238000000926 separation method Methods 0.000 abstract description 5
- 239000002351 wastewater Substances 0.000 abstract description 5
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 abstract description 4
- 239000006185 dispersion Substances 0.000 abstract description 4
- 229910052799 carbon Inorganic materials 0.000 abstract description 3
- 239000007788 liquid Substances 0.000 abstract description 3
- 230000003647 oxidation Effects 0.000 abstract description 2
- 238000007254 oxidation reaction Methods 0.000 abstract description 2
- 238000011084 recovery Methods 0.000 abstract description 2
- 239000011248 coating agent Substances 0.000 abstract 2
- 238000000576 coating method Methods 0.000 abstract 2
- 239000013543 active substance Substances 0.000 abstract 1
- 238000004065 wastewater treatment Methods 0.000 abstract 1
- 239000008367 deionised water Substances 0.000 description 24
- 229910021641 deionized water Inorganic materials 0.000 description 24
- 235000021317 phosphate Nutrition 0.000 description 18
- 230000000694 effects Effects 0.000 description 12
- 230000000052 comparative effect Effects 0.000 description 11
- 238000007885 magnetic separation Methods 0.000 description 10
- 239000012265 solid product Substances 0.000 description 8
- APUPEJJSWDHEBO-UHFFFAOYSA-P ammonium molybdate Chemical compound [NH4+].[NH4+].[O-][Mo]([O-])(=O)=O APUPEJJSWDHEBO-UHFFFAOYSA-P 0.000 description 7
- 239000011609 ammonium molybdate Substances 0.000 description 7
- 229940010552 ammonium molybdate Drugs 0.000 description 7
- 235000018660 ammonium molybdate Nutrition 0.000 description 7
- 238000002798 spectrophotometry method Methods 0.000 description 7
- 238000012360 testing method Methods 0.000 description 7
- 238000010586 diagram Methods 0.000 description 6
- MRELNEQAGSRDBK-UHFFFAOYSA-N lanthanum(3+);oxygen(2-) Chemical compound [O-2].[O-2].[O-2].[La+3].[La+3] MRELNEQAGSRDBK-UHFFFAOYSA-N 0.000 description 5
- 230000004048 modification Effects 0.000 description 5
- 238000012986 modification Methods 0.000 description 5
- 239000002245 particle Substances 0.000 description 5
- 239000007787 solid Substances 0.000 description 5
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 4
- 238000001816 cooling Methods 0.000 description 4
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 3
- 150000002604 lanthanum compounds Chemical class 0.000 description 3
- YXEUGTSPQFTXTR-UHFFFAOYSA-K lanthanum(3+);trihydroxide Chemical compound [OH-].[OH-].[OH-].[La+3] YXEUGTSPQFTXTR-UHFFFAOYSA-K 0.000 description 3
- 238000010907 mechanical stirring Methods 0.000 description 3
- 229940057838 polyethylene glycol 4000 Drugs 0.000 description 3
- 239000000047 product Substances 0.000 description 3
- 239000000758 substrate Substances 0.000 description 3
- 238000005406 washing Methods 0.000 description 3
- 239000011149 active material Substances 0.000 description 2
- 238000005054 agglomeration Methods 0.000 description 2
- 230000002776 aggregation Effects 0.000 description 2
- 150000001875 compounds Chemical class 0.000 description 2
- 150000003013 phosphoric acid derivatives Chemical class 0.000 description 2
- 238000000746 purification Methods 0.000 description 2
- 238000006467 substitution reaction Methods 0.000 description 2
- 241000894006 Bacteria Species 0.000 description 1
- 239000002028 Biomass Substances 0.000 description 1
- 241000195493 Cryptophyta Species 0.000 description 1
- 241000196324 Embryophyta Species 0.000 description 1
- 241001465754 Metazoa Species 0.000 description 1
- 229910004298 SiO 2 Inorganic materials 0.000 description 1
- WKUCEDMXGGPQFH-UHFFFAOYSA-K [OH-].[OH-].[OH-].O.O.O.P.[La+3] Chemical compound [OH-].[OH-].[OH-].O.O.O.P.[La+3] WKUCEDMXGGPQFH-UHFFFAOYSA-K 0.000 description 1
- 239000000853 adhesive Substances 0.000 description 1
- 230000001476 alcoholic effect Effects 0.000 description 1
- 150000001450 anions Chemical class 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000009388 chemical precipitation Methods 0.000 description 1
- 239000007795 chemical reaction product Substances 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 239000011247 coating layer Substances 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 230000006866 deterioration Effects 0.000 description 1
- 238000011161 development Methods 0.000 description 1
- 229940079593 drug Drugs 0.000 description 1
- 239000003814 drug Substances 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000012851 eutrophication Methods 0.000 description 1
- 125000000524 functional group Chemical group 0.000 description 1
- 239000010439 graphite Substances 0.000 description 1
- 229910002804 graphite Inorganic materials 0.000 description 1
- 230000002209 hydrophobic effect Effects 0.000 description 1
- 201000005991 hyperphosphatemia Diseases 0.000 description 1
- -1 lanthanum carbonate-modified Fe3O4 Chemical class 0.000 description 1
- 231100000053 low toxicity Toxicity 0.000 description 1
- 239000012528 membrane Substances 0.000 description 1
- 238000006116 polymerization reaction Methods 0.000 description 1
- 230000008569 process Effects 0.000 description 1
- 229910052761 rare earth metal Inorganic materials 0.000 description 1
- 230000009467 reduction Effects 0.000 description 1
- 230000002195 synergetic effect Effects 0.000 description 1
- 238000001291 vacuum drying Methods 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- 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
- B01J20/02—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material
- B01J20/0203—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material comprising compounds of metals not provided for in B01J20/04
- B01J20/0207—Compounds of Sc, Y or Lanthanides
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- 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
- B01J20/02—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material
- B01J20/0203—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material comprising compounds of metals not provided for in B01J20/04
- B01J20/0274—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material comprising compounds of metals not provided for in B01J20/04 characterised by the type of anion
- B01J20/0277—Carbonates of compounds other than those provided for in B01J20/043
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- 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
- B01J20/02—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material
- B01J20/06—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material comprising oxides or hydroxides of metals not provided for in group B01J20/04
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- 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
- B01J20/02—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material
- B01J20/20—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material comprising free carbon; comprising carbon obtained by carbonising processes
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- 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
- B01J20/28—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof characterised by their form or physical properties
- B01J20/28002—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof characterised by their form or physical properties characterised by their physical properties
- B01J20/28009—Magnetic properties
-
- 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
- C02F1/288—Treatment of water, waste water, or sewage by sorption using composite sorbents, e.g. coated, impregnated, multi-layered
-
- 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
- C02F2101/105—Phosphorus compounds
-
- 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
- C02F2101/30—Organic compounds
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W10/00—Technologies for wastewater treatment
- Y02W10/10—Biological treatment of water, waste water, or sewage
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Analytical Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Inorganic Chemistry (AREA)
- Life Sciences & Earth Sciences (AREA)
- Hydrology & Water Resources (AREA)
- Engineering & Computer Science (AREA)
- Environmental & Geological Engineering (AREA)
- Water Supply & Treatment (AREA)
- Solid-Sorbent Or Filter-Aiding Compositions (AREA)
Abstract
本发明属于环境废水处理领域,公开了一种碳酸镧改性Fe3O4@C复合吸附材料及其制备方法和应用。该吸附剂的制备方法包括以下步骤:利用溶剂热法制备Fe3O4纳米颗粒;再将Fe3O4用水热法包覆一层碳层;最后利用沉淀沉积法在Fe3O4@C载体上负载碳酸镧,得到复合除磷吸附剂。本发明具有很强的磁性,吸附剂可在吸附结束后外加磁场进行固液分离回收。碳包覆使得Fe3O4不易被氧化,且提高了材料活性物质的分散性;碳酸镧对磷酸盐有极强的亲和力,可以对酸性或中性的含磷废水实现高效吸附。
The invention belongs to the field of environmental wastewater treatment and discloses a lanthanum carbonate-modified Fe 3 O 4 @C composite adsorption material and its preparation method and application. The preparation method of the adsorbent includes the following steps: using a solvothermal method to prepare Fe 3 O 4 nanoparticles; then coating Fe 3 O 4 with a carbon layer using a hydrothermal method; and finally using a precipitation deposition method to coat Fe 3 O 4 @C Lanthanum carbonate is loaded on the carrier to obtain a composite phosphorus removal adsorbent. The invention has strong magnetism, and the adsorbent can perform solid-liquid separation and recovery by applying an external magnetic field after the adsorption is completed. Carbon coating makes Fe 3 O 4 less susceptible to oxidation and improves the dispersion of the material's active substances; lanthanum carbonate has a strong affinity for phosphate and can achieve efficient adsorption of acidic or neutral phosphorus-containing wastewater.
Description
技术领域Technical field
本发明属于环境吸附领域,特别涉及一种碳酸镧改性Fe3O4@C除磷吸附剂及其制备方法和应用。The invention belongs to the field of environmental adsorption, and particularly relates to a lanthanum carbonate-modified Fe 3 O 4 @C phosphorus removal adsorbent and its preparation method and application.
背景技术Background technique
磷是人类及各种动植物、细菌生命活动的重要元素,但是大量的含磷废水排放可能会导致水体的富营养化。磷的自然循环是十分缓慢的,富营养化的水体会引起藻类繁殖、水质恶化、水生生物死亡等一系列环境问题。因此,对含磷废水进行处理十分必要。Phosphorus is an important element for the life activities of humans, various animals, plants, and bacteria, but the discharge of large amounts of phosphorus-containing wastewater may lead to eutrophication of water bodies. The natural cycle of phosphorus is very slow. Eutrophic water bodies can cause a series of environmental problems such as algae reproduction, deterioration of water quality, and death of aquatic organisms. Therefore, it is very necessary to treat phosphorus-containing wastewater.
当前已经研发出很多种水体除磷的方法,包括化学沉淀法、膜分离法、生物法以及吸附法等。在众多的方法中,吸附法由于操作简单、成本低、适用范围广以及无二次污染等优点而被广泛关注。Many methods for phosphorus removal from water have been developed, including chemical precipitation, membrane separation, biological and adsorption methods. Among many methods, the adsorption method has attracted widespread attention due to its advantages such as simple operation, low cost, wide application range, and no secondary pollution.
镧是地球上相对丰富、环境友好的稀土元素之一。镧及其化合物对磷有特异的吸附性能,即使在痕量的情况下都有很强的亲和力。目前,在环境除磷剂中常用的活性镧化合物是氢氧化镧或氧化镧。例如中国专利公开文本CN104722271A公布的一种膨胀石墨负载氢氧化镧除磷吸附剂;中国专利公开文本CN105214629A公布的一种生物质基纳米氧化镧除磷复合吸附剂。但这两种镧化合物在与磷酸盐结合时,会由于配位交换使得溶液pH快速增加,从而导致其吸附效率明显降低。因此,改变镧化合物中的阴离子,减少吸附过程中由于pH的改变对体系的影响,是提高吸附剂除磷效率的方法之一。Lanthanum is one of the relatively abundant and environmentally friendly rare earth elements on Earth. Lanthanum and its compounds have specific adsorption properties for phosphorus and have a strong affinity even in trace amounts. Currently, the most commonly used active lanthanum compounds in environmental phosphorus removal agents are lanthanum hydroxide or lanthanum oxide. For example, Chinese patent publication CN104722271A discloses an expanded graphite-loaded lanthanum hydroxide phosphorus removal adsorbent; Chinese patent publication CN105214629A discloses a biomass-based nano-lanthanum oxide phosphorus removal composite adsorbent. However, when these two lanthanum compounds are combined with phosphate, the pH of the solution will rapidly increase due to coordination exchange, resulting in a significant reduction in their adsorption efficiency. Therefore, changing the anions in lanthanum compounds and reducing the impact of pH changes on the system during the adsorption process is one of the methods to improve the phosphorus removal efficiency of adsorbents.
碳酸镧是镧的另一种化合物形态,它高度难溶,且在和磷酸盐进行交换时对溶液的pH影响较小。碳酸镧因为对人类和生物有着相对较低的毒性,现已经被美国食品和药物管理局(FDA)批准为治疗高磷血症的粘合药剂。尽管碳酸镧在医学领域已经得到很好研究,但应用于环境含磷废水处理中的报导还比较少。Lanthanum carbonate is another compound form of lanthanum. It is highly insoluble and has little effect on the pH of the solution when exchanged with phosphate. Lanthanum carbonate has been approved by the U.S. Food and Drug Administration (FDA) as an adhesive agent for the treatment of hyperphosphatemia because of its relatively low toxicity to humans and organisms. Although lanthanum carbonate has been well studied in the medical field, there are relatively few reports on its application in the treatment of environmental phosphorus-containing wastewater.
传统的吸附剂在使用时会存在难以分离再生的问题,开发一种磁性复合材料是很好的解决办法。Fe3O4由于具有强磁性、制备工艺简单等优点而被广泛应用。遗憾的是,Fe3O4在空气中容易发生氧化,进而导致粒子发生团聚、磁性减弱。为了克服这一点,很多研究者尝试对Fe3O4颗粒的表面覆盖一层惰性壳层,这种方法在防止Fe3O4氧化的同时,还使得材料产生空间位阻斥力,提高复合吸附剂的分散性及比表面积。例如中国专利公开文本CN103964538A公布了一种CeO2改性的SiO2包覆Fe3O4磁性磷吸附剂。但该公开文本的磷酸盐吸附效果明显弱于其他专利中的镧化合物改性的吸附剂。Traditional adsorbents have the problem of being difficult to separate and regenerate during use. The development of a magnetic composite material is a good solution. Fe 3 O 4 is widely used due to its strong magnetism and simple preparation process. Unfortunately, Fe 3 O 4 is easily oxidized in the air, leading to particle agglomeration and weakened magnetism. In order to overcome this, many researchers have tried to cover the surface of Fe 3 O 4 particles with an inert shell. This method not only prevents the oxidation of Fe 3 O 4 , but also causes the material to generate steric repulsion and improves the composite adsorbent. dispersion and specific surface area. For example, Chinese patent publication CN103964538A discloses a CeO 2 modified SiO 2 coated Fe 3 O 4 magnetic phosphorus adsorbent. However, the phosphate adsorption effect of this publication is significantly weaker than that of the lanthanum compound-modified adsorbent in other patents.
发明内容Contents of the invention
为了克服上述现有技术的缺点与不足,本发明的首要目的在于提供一种碳酸镧改性Fe3O4@C除磷吸附剂的制备方法。In order to overcome the shortcomings and deficiencies of the above-mentioned prior art, the primary purpose of the present invention is to provide a method for preparing a lanthanum carbonate-modified Fe 3 O 4 @C phosphorus removal adsorbent.
本发明的另一个目的在于提供上述方法制备的碳酸镧改性Fe3O4@C除磷吸附剂,该吸附剂不仅吸附性能强,而且还具有强磁性,方便分离回收。Another object of the present invention is to provide a lanthanum carbonate-modified Fe 3 O 4 @C phosphorus removal adsorbent prepared by the above method. The adsorbent not only has strong adsorption performance, but also has strong magnetism and is convenient for separation and recovery.
本发明的再一个目的在于提供上述碳酸镧改性Fe3O4@C除磷吸附剂在磷酸盐吸附中的应用。Another object of the present invention is to provide the application of the above-mentioned lanthanum carbonate modified Fe 3 O 4 @C phosphorus removal adsorbent in phosphate adsorption.
本发明的目的通过下述方案实现:The object of the present invention is achieved through the following solutions:
一种碳酸镧改性Fe3O4@C除磷吸附剂的制备方法,包括以下步骤:A preparation method of lanthanum carbonate modified Fe 3 O 4 @C phosphorus removal adsorbent, including the following steps:
(1)溶剂热法制备Fe3O4纳米颗粒:将铁盐加入到乙二醇溶剂中超声溶解,再加入无水乙酸钠,聚乙二醇,搅拌溶解后,转移到反应釜中反应,将所得产物纯化即得到Fe3O4纳米颗粒;(1) Preparation of Fe 3 O 4 nanoparticles by solvothermal method: Add the iron salt to the ethylene glycol solvent and dissolve it with ultrasound, then add anhydrous sodium acetate and polyethylene glycol, stir and dissolve, then transfer to the reaction kettle for reaction. The obtained product is purified to obtain Fe 3 O 4 nanoparticles;
(2)水热法制备Fe3O4@C材料:将步骤(1)制备的Fe3O4纳米颗粒均匀分散于水中,加入葡萄糖或蔗糖,搅拌均匀后转移至反应釜中进行水热反应,将所得产物纯化即得Fe3O4@C;(2) Preparation of Fe 3 O 4 @C material by hydrothermal method: Evenly disperse the Fe 3 O 4 nanoparticles prepared in step (1) in water, add glucose or sucrose, stir evenly and transfer to a reactor for hydrothermal reaction. , the obtained product is purified to obtain Fe 3 O 4 @C;
(3)沉淀沉积法制备碳酸镧改性Fe3O4@C材料:将镧盐超声溶解在水中,再加入步骤(2)制备的Fe3O4@C,振荡搅拌混合均匀,滴加碳酸氢盐水溶液,直至pH为中性,将所得悬浮液静置一晚,然后洗涤并干燥即得碳酸镧改性的Fe3O4@C材料。(3) Preparation of lanthanum carbonate modified Fe 3 O 4 @C material by precipitation deposition method: Dissolve the lanthanum salt in water ultrasonically, then add the Fe 3 O 4 @C prepared in step (2), oscillate and stir to mix evenly, and add carbonic acid dropwise Hydrogen aqueous salt solution until the pH is neutral, and the resulting suspension is allowed to stand overnight, then washed and dried to obtain the lanthanum carbonate-modified Fe 3 O 4 @C material.
步骤(1)中所述的铁盐为FeCl3·6H2O,Fe(NO3)3·9H2O,Fe2(SO4)3·9H2O中的至少一种。The iron salt described in step (1) is at least one of FeCl 3 ·6H 2 O, Fe(NO 3 ) 3 ·9H 2 O, and Fe 2 (SO 4 ) 3 ·9H 2 O.
步骤(1)中所述的铁盐与乙二醇的用量满足每1~4mmol的铁盐对应加入到30-50ml的乙二醇中;优选为每2mmol的铁盐对应加入到40ml的乙二醇中。The amount of iron salt and ethylene glycol described in step (1) is such that every 1 to 4 mmol of iron salt is added to 30-50 ml of ethylene glycol; preferably, every 2 mmol of iron salt is added to 40 ml of ethylene glycol. Alcoholic.
步骤(1)中所述的铁盐、无水乙酸钠,聚乙二醇的用量满足:每1~4mmol的铁盐对应加入0.5~1g的聚乙二醇和2.4-7.2g的无水乙酸钠;步骤(1)中的聚乙二醇的聚合度为500~10000。The amount of iron salt, anhydrous sodium acetate, and polyethylene glycol described in step (1) satisfies: for every 1 to 4 mmol of iron salt, add 0.5 to 1 g of polyethylene glycol and 2.4 to 7.2 g of anhydrous sodium acetate. ; The degree of polymerization of polyethylene glycol in step (1) is 500 to 10,000.
步骤(1)中所述的搅拌溶解的时间优选为30~120min。The stirring and dissolving time described in step (1) is preferably 30 to 120 minutes.
步骤(1)中所述的反应是指将反应釜置于150~220℃的烘箱中进行反应,优选为在200℃的烘箱中反应;步骤(1)中所述的反应时间为8-16h,优选为12h。The reaction described in step (1) refers to placing the reaction kettle in an oven at 150-220°C for reaction, preferably in an oven at 200°C; the reaction time described in step (1) is 8-16h , preferably 12h.
步骤(1)中所述的纯化是指反应结束后,将所得产物自然冷却后磁分离取固体产物,用去离子水和无水乙醇洗涤各三次并干燥后,即得纯化后的Fe3O4纳米颗粒,其中干燥优选为真空干燥,干燥温度为60~100℃,干燥时间为8~12h。The purification described in step (1) means that after the reaction is completed, the obtained product is naturally cooled and then magnetically separated to collect the solid product. After washing three times with deionized water and absolute ethanol and drying, the purified Fe 3 O is obtained. 4 nanoparticles, the drying is preferably vacuum drying, the drying temperature is 60-100°C, and the drying time is 8-12 hours.
步骤(2)中所述的Fe3O4纳米颗粒在分散于水中之前,优选为先分散于HNO3溶液中,然后经磁分离、水洗涤后再分散于水中,其中HNO3溶液的浓度优选为1mol/L。Fe3O4是疏水的,用HNO3处理是为了Fe3O4引入亲水官能团,使得Fe3O4易于被葡萄糖或蔗糖包覆。Before being dispersed in water, the Fe 3 O 4 nanoparticles described in step (2) are preferably first dispersed in an HNO 3 solution, and then magnetically separated and washed with water before being dispersed in the water, wherein the concentration of the HNO 3 solution is preferably is 1mol/L. Fe 3 O 4 is hydrophobic, and treatment with HNO 3 is to introduce hydrophilic functional groups into Fe 3 O 4 , making it easy for Fe 3 O 4 to be coated with glucose or sucrose.
步骤(2)中所述的葡萄糖或蔗糖的用量满足:每1g的Fe3O4纳米颗粒对应加入2~4g的葡萄糖或蔗糖。The amount of glucose or sucrose described in step (2) is such that for every 1 g of Fe 3 O 4 nanoparticles, 2 to 4 g of glucose or sucrose are added.
步骤(2)中所述的水热反应是在是指在150~220℃的烘箱中进行反应,优选为200℃;步骤(2)中所述的水热时间为8~16h,优选为12h。The hydrothermal reaction described in step (2) refers to the reaction in an oven at 150-220°C, preferably 200°C; the hydrothermal time described in step (2) is 8-16h, preferably 12h .
步骤(2)中所述的纯化是指将反应后的产物自然冷却后磁分离取固体产物,用去离子水洗涤三次并干燥后,得到纯化后的Fe3O4@C,其中干燥优选为鼓风干燥,干燥温度为60~100℃,干燥时间为8~12h。The purification described in step (2) refers to cooling the reaction product naturally, magnetically separating the solid product, washing it three times with deionized water and drying to obtain purified Fe 3 O 4 @C, where the drying is preferably Air blast drying, drying temperature is 60~100℃, drying time is 8~12h.
步骤(3)中所述的镧盐为LaCl3·7H2O,La(NO3)3·6H2O,La2(SO4)3·9H2O的至少一种。The lanthanum salt described in step (3) is at least one of LaCl 3 ·7H 2 O, La(NO 3 ) 3 ·6H 2 O, and La 2 (SO 4 ) 3 ·9H 2 O.
步骤(3)中所述的镧盐与Fe3O4@C的用量满足:镧盐中La3+的质量与Fe3O4@C的质量比为0.5~2:1。The dosage of the lanthanum salt and Fe 3 O 4 @C described in step (3) satisfies: the mass ratio of the mass of La 3+ in the lanthanum salt to Fe 3 O 4 @C is 0.5 to 2:1.
步骤(3)中所述的碳酸氢盐优选为NaHCO3、KHCO3、NH4HCO3的至少一种;步骤(3)中所述的碳酸氢盐水溶液的浓度优选为1mol/L;滴加速度为0.2~1ml/min,优选为0.4ml/min。The bicarbonate salt described in step (3) is preferably at least one of NaHCO 3 , KHCO 3 , and NH 4 HCO 3 ; the concentration of the bicarbonate aqueous solution described in step (3) is preferably 1 mol/L; the dripping speed It is 0.2~1ml/min, preferably 0.4ml/min.
步骤(3)中所述的干燥为鼓风干燥,干燥温度为60~100℃,干燥时间为8~12h。The drying described in step (3) is blast drying, the drying temperature is 60 to 100°C, and the drying time is 8 to 12 hours.
一种由上述方法制备得到的碳酸镧改性Fe3O4@C除磷吸附剂。A lanthanum carbonate-modified Fe 3 O 4 @C phosphorus removal adsorbent prepared by the above method.
上述碳酸镧改性Fe3O4@C除磷吸附剂在酸性或中性条件下吸附磷酸盐中的应用。Application of the above lanthanum carbonate modified Fe 3 O 4 @C phosphorus removal adsorbent in adsorbing phosphate under acidic or neutral conditions.
本发明相对于现有技术,具有如下的优点及有益效果:Compared with the existing technology, the present invention has the following advantages and beneficial effects:
(1)所制备的吸附剂对水体中的磷酸盐具有很高的吸附容量。如附图2,本发明的吸附剂对磷酸盐的吸附更符合Langmuir模型,该模型计算得到在吸附剂投加量为0.4g/L,溶液pH=7±0.1,吸附温度为298K的吸附条件下最大理论吸附量可达74.63mg-P/g。(1) The prepared adsorbent has a high adsorption capacity for phosphates in water. As shown in Figure 2, the adsorption of phosphate by the adsorbent of the present invention is more consistent with the Langmuir model. The model calculates the adsorption conditions when the adsorbent dosage is 0.4g/L, the solution pH=7±0.1, and the adsorption temperature is 298K. The maximum theoretical adsorption capacity can reach 74.63mg-P/g.
(2)在酸性或中性的条件下有很好的吸附性能,见附图3。(2) It has good adsorption performance under acidic or neutral conditions, see Figure 3.
(3)吸附剂具有强磁性,可以方便地进行固液分离操作,见附图4。(3) The adsorbent has strong magnetism and can easily perform solid-liquid separation operations, see Figure 4.
(4)相对于常见的氢氧化镧或氧化镧,本发明运用了对磷酸盐有更好吸附性能的碳酸镧进行改性。(4) Compared with common lanthanum hydroxide or lanthanum oxide, the present invention uses lanthanum carbonate with better adsorption performance for phosphates for modification.
(5)碳包覆层有效保护了Fe3O4纳米颗粒,防止Fe3O4在空气或水体中被氧化。Fe3O4@C基底有一定的分散作用,避免了活性物质碳酸镧的团聚。(5) The carbon coating layer effectively protects Fe 3 O 4 nanoparticles and prevents Fe 3 O 4 from being oxidized in air or water. The Fe 3 O 4 @C substrate has a certain dispersion effect and avoids the agglomeration of the active material lanthanum carbonate.
附图说明Description of the drawings
图1为实施例1-4以及对比例1-3中吸附剂对磷酸盐的吸附性能对比图。Figure 1 is a comparison chart of the adsorption performance of the adsorbents on phosphate in Examples 1-4 and Comparative Examples 1-3.
图2为实施例2中对应材料的等温吸附线图(吸附剂投加量为0.4g/L,溶液初始pH=7±0.1,吸附温度为298K)Figure 2 is the isothermal adsorption line diagram of the corresponding material in Example 2 (adsorbent dosage is 0.4g/L, initial pH of the solution=7±0.1, adsorption temperature is 298K)
图3为实施例2中对应材料在不同初始pH下的吸附量图(吸附剂投加量为0.4g/L,溶液初始浓度为50mg-P/L,吸附温度为298K)Figure 3 is a diagram of the adsorption capacity of the corresponding materials in Example 2 under different initial pH (adsorbent dosage is 0.4g/L, initial solution concentration is 50mg-P/L, adsorption temperature is 298K)
图4为实施例2中对应材料的磁性分离图。Figure 4 is a magnetic separation diagram of the corresponding material in Example 2.
具体实施方式Detailed ways
下面结合实施例和附图对本发明作进一步详细的描述,但本发明的实施方式不限于此。凡是采用了本发明相似结构或相似变化,均应列入本发明的保护范围之内。The present invention will be described in further detail below with reference to the examples and drawings, but the implementation of the present invention is not limited thereto. All similar structures or similar changes of the present invention should be included in the protection scope of the present invention.
实施例1Example 1
La3+:Fe3O4@C质量比为0.5:1的碳酸镧改性Fe3O4@C复合材料制备方法,包括以下步骤:A method for preparing a lanthanum carbonate-modified Fe 3 O 4 @C composite material with a La 3+ : Fe 3 O 4 @C mass ratio of 0.5:1, including the following steps:
(1)2mmol FeCl3·6H2O加入到40ml乙二醇溶剂中超声溶解,加入1g聚乙二醇4000,3.6g无水乙酸钠,磁力搅拌30min后转移到反应釜中200℃下反应12h,自然冷却,磁分离,固体产物用去离子水和无水乙醇洗涤各三次,60℃下真空干燥12h,得到Fe3O4纳米颗粒。(1) 2 mmol FeCl 3 ·6H 2 O was added to 40 ml of ethylene glycol solvent and dissolved by ultrasound. Add 1 g of polyethylene glycol 4000 and 3.6 g of anhydrous sodium acetate. Stir magnetically for 30 min and then transfer to a reaction kettle at 200°C for 12 h. , natural cooling, magnetic separation, the solid product was washed three times each with deionized water and absolute ethanol, and vacuum dried at 60°C for 12 hours to obtain Fe 3 O 4 nanoparticles.
(2)将1g步骤(1)制备的Fe3O4在0.1mol/LHNO3溶液中超声分散10min后,磁分离,去离子水洗涤三次后,将颗粒机械搅拌分散在30ml去离子水中。在上述悬浊液中加入2g葡萄糖,机械搅拌10min后,将溶液转移到反应釜中,200℃下反应12小时,自然冷却,磁分离,固体产物用去离子水洗涤三次后60℃干燥12h,得到Fe3O4@C备用。(2) Disperse 1 g of Fe 3 O 4 prepared in step (1) ultrasonically in a 0.1 mol/LHNO 3 solution for 10 minutes, magnetically separate, wash three times with deionized water, and disperse the particles in 30 ml of deionized water with mechanical stirring. Add 2g glucose to the above suspension, stir mechanically for 10 minutes, transfer the solution to the reactor, react at 200°C for 12 hours, cool naturally, and magnetically separate. The solid product is washed three times with deionized water and dried at 60°C for 12 hours. Obtain Fe 3 O 4 @C for later use.
(3)将0.743gLaCl3·7H2O超声溶解在50ml去离子水中,加入0.556g步骤(2)制得的Fe3O4@C,在恒温振荡器中振荡搅拌4h。边快速机械搅拌,边以0.4ml/min的速度往上述悬浊液中滴加1mol/LNaHCO3溶液,直至pH为中性,静置一晚。磁分离后固体用去离子水洗涤三次,60℃下干燥12h。(3) Dissolve 0.743g LaCl 3 ·7H 2 O in 50 ml deionized water by ultrasonic, add 0.556g Fe 3 O 4 @C prepared in step (2), and oscillate and stir in a constant temperature oscillator for 4 hours. While rapidly mechanically stirring, add 1 mol/L NaHCO 3 solution dropwise to the above suspension at a speed of 0.4 ml/min until the pH is neutral, and let it stand overnight. After magnetic separation, the solid was washed three times with deionized water and dried at 60°C for 12 h.
吸附剂活性测试:Adsorbent activity test:
向一100ml锥形瓶中,加入50ml,浓度为50mg-P/L,pH=7.0±0.1的KH2PO4溶液。用0.02gLa3+:Fe3O4@C质量比为0.5:1的碳酸镧改性Fe3O4@C复合材料进行吸附。吸附条件为298K的温度、200rpm的转速下恒温振荡24h。To a 100 ml Erlenmeyer flask, add 50 ml of KH 2 PO 4 solution with a concentration of 50 mg-P/L and pH=7.0±0.1. The lanthanum carbonate-modified Fe 3 O 4 @C composite material with a mass ratio of 0.02gLa 3+ :Fe 3 O 4 @C is 0.5:1 was used for adsorption. The adsorption conditions were a temperature of 298K and a rotation speed of 200rpm with constant temperature shaking for 24h.
反应结束后,用钼酸铵分光光度法进行分析,结果表明,磷酸盐的吸附量为50.90mg-P/g。After the reaction, the ammonium molybdate spectrophotometric method was used for analysis. The results showed that the adsorption capacity of phosphate was 50.90mg-P/g.
实施例2Example 2
La3+:Fe3O4@C质量比为1:1的碳酸镧改性Fe3O4@C复合材料制备方法,包括以下步骤:A method for preparing a lanthanum carbonate-modified Fe 3 O 4 @C composite material with a La 3+ : Fe 3 O 4 @C mass ratio of 1:1, including the following steps:
(1)2mmolFeCl3·6H2O加入到40ml乙二醇溶剂中超声溶解,加入1g聚乙二醇4000,3.6g无水乙酸钠,磁力搅拌30min后转移到反应釜中200℃下反应12h,自然冷却,磁分离,固体产物用去离子水和无水乙醇洗涤各三次,60℃下真空干燥12h,得到Fe3O4纳米颗粒。(1) 2 mmol FeCl 3 ·6H 2 O was added to 40 ml of ethylene glycol solvent and dissolved by ultrasound. Add 1 g of polyethylene glycol 4000 and 3.6 g of anhydrous sodium acetate. Stir magnetically for 30 min and then transfer to a reaction kettle to react at 200°C for 12 h. After natural cooling, magnetic separation, the solid product was washed three times each with deionized water and absolute ethanol, and vacuum dried at 60°C for 12 hours to obtain Fe 3 O 4 nanoparticles.
(2)将1g步骤(1)制备的Fe3O4在0.1mol/LHNO3溶液中超声分散10min后,磁分离,去离子水洗涤三次后,将颗粒机械搅拌分散在30ml去离子水中。在上述悬浊液中加入2g葡萄糖,机械搅拌10min后,将溶液转移到反应釜中,200℃下反应12小时,自然冷却,磁分离,固体产物用去离子水洗涤三次后60℃干燥12h,得到Fe3O4@C备用。(2) Disperse 1 g of Fe 3 O 4 prepared in step (1) ultrasonically in a 0.1 mol/LHNO 3 solution for 10 minutes, magnetically separate, wash three times with deionized water, and disperse the particles in 30 ml of deionized water with mechanical stirring. Add 2g glucose to the above suspension, stir mechanically for 10 minutes, transfer the solution to the reactor, react at 200°C for 12 hours, cool naturally, and magnetically separate. The solid product is washed three times with deionized water and dried at 60°C for 12 hours. Obtain Fe 3 O 4 @C for later use.
(3)将1.486g LaCl3·7H2O超声溶解在50ml去离子水中,加入0.556g步骤(2)制得的Fe3O4@C,在恒温振荡器中振荡搅拌4h。边快速机械搅拌,边以0.4ml/min的速度往上述悬浊液中滴加1mol/L NaHCO3溶液,直至pH为中性,静置一晚。磁分离后固体用去离子水洗涤三次,60℃下干燥12h。(3) Dissolve 1.486g LaCl 3 ·7H 2 O in 50 ml deionized water under ultrasonic, add 0.556g Fe 3 O 4 @C prepared in step (2), and oscillate and stir in a constant temperature oscillator for 4 hours. While rapidly mechanically stirring, add 1 mol/L NaHCO 3 solution dropwise to the above suspension at a speed of 0.4 ml/min until the pH is neutral, and let it stand overnight. After magnetic separation, the solid was washed three times with deionized water and dried at 60°C for 12 h.
吸附剂活性测试:Adsorbent activity test:
向一100ml锥形瓶中,加入50ml,浓度为50mg-P/L,pH=7.0±0.1的KH2PO4溶液。用0.02gLa3+:Fe3O4@C质量比为1:1的碳酸镧改性Fe3O4@C复合材料进行吸附。吸附条件为298K的温度、200rpm的转速下恒温振荡24h。To a 100 ml Erlenmeyer flask, add 50 ml of KH 2 PO 4 solution with a concentration of 50 mg-P/L and pH=7.0±0.1. The lanthanum carbonate-modified Fe 3 O 4 @C composite material with a mass ratio of 0.02gLa 3+ :Fe 3 O 4 @C is 1:1 was used for adsorption. The adsorption conditions were a temperature of 298K and a rotation speed of 200rpm with constant temperature shaking for 24h.
反应结束后,用钼酸铵分光光度法进行分析,结果表明,磷酸盐的吸附量为63.64mg-P/g。After the reaction, the ammonium molybdate spectrophotometric method was used for analysis. The results showed that the adsorption capacity of phosphate was 63.64mg-P/g.
实施例3Example 3
La3+:Fe3O4@C质量比为2:1的碳酸镧改性Fe3O4@C复合材料制备方法,包括以下步骤:A method for preparing a lanthanum carbonate-modified Fe 3 O 4 @C composite material with a La 3+ : Fe 3 O 4 @C mass ratio of 2:1, including the following steps:
(1)2mmol FeCl3·6H2O加入到40ml乙二醇溶剂中超声溶解,加入1g聚乙二醇4000,3.6g无水乙酸钠,磁力搅拌30min后转移到反应釜中200℃下反应12h,自然冷却,磁分离,固体产物用去离子水和无水乙醇洗涤各三次,60℃下真空干燥12h,得到Fe3O4纳米颗粒。(1) 2 mmol FeCl 3 ·6H 2 O was added to 40 ml of ethylene glycol solvent and dissolved by ultrasound. Add 1 g of polyethylene glycol 4000 and 3.6 g of anhydrous sodium acetate. Stir magnetically for 30 min and then transfer to a reaction kettle at 200°C for 12 h. , natural cooling, magnetic separation, the solid product was washed three times each with deionized water and absolute ethanol, and vacuum dried at 60°C for 12 hours to obtain Fe 3 O 4 nanoparticles.
(2)将1g步骤(1)制备的Fe3O4在0.1mol/L HNO3溶液中超声分散10min后,磁分离,去离子水洗涤三次后,将颗粒机械搅拌分散在30ml去离子水中。在上述悬浊液中加入2g葡萄糖,机械搅拌10min后,将溶液转移到反应釜中,200℃下反应12小时,自然冷却,磁分离,固体产物用去离子水洗涤三次后60℃干燥12h,得到Fe3O4@C备用。(2) Disperse 1 g of Fe 3 O 4 prepared in step (1) ultrasonically in a 0.1 mol/L HNO 3 solution for 10 minutes, then magnetically separate. After washing with deionized water three times, the particles are mechanically stirred and dispersed in 30 ml of deionized water. Add 2g glucose to the above suspension, stir mechanically for 10 minutes, transfer the solution to the reactor, react at 200°C for 12 hours, cool naturally, and magnetically separate. The solid product is washed three times with deionized water and dried at 60°C for 12 hours. Obtain Fe 3 O 4 @C for later use.
(3)将2.972gLaCl3·7H2O超声溶解在50ml去离子水中,加入0.556g步骤(2)制得的Fe3O4@C,在恒温振荡器中振荡搅拌4h。边快速机械搅拌,边以0.4ml/min的速度往上述悬浊液中滴加1mol/LNaHCO3溶液,直至pH为中性,静置一晚。磁分离后固体用去离子水洗涤三次,60℃下干燥12h。(3) Dissolve 2.972g LaCl 3 ·7H 2 O in 50 ml deionized water under ultrasonic, add 0.556g Fe 3 O 4 @C prepared in step (2), and oscillate and stir in a constant temperature oscillator for 4 hours. While rapidly mechanically stirring, add 1 mol/L NaHCO 3 solution dropwise to the above suspension at a speed of 0.4 ml/min until the pH is neutral, and let it stand overnight. After magnetic separation, the solid was washed three times with deionized water and dried at 60°C for 12 h.
吸附剂活性测试:Adsorbent activity test:
向一100ml锥形瓶中,加入50ml,浓度为50mg-P/L,pH=7.0±0.1的KH2PO4溶液。用0.02gLa3+:Fe3O4@C质量比为2:1的碳酸镧改性Fe3O4@C复合材料进行吸附。吸附条件为298K的温度、200rpm的转速下恒温振荡24h。To a 100 ml Erlenmeyer flask, add 50 ml of KH 2 PO 4 solution with a concentration of 50 mg-P/L and pH=7.0±0.1. The lanthanum carbonate-modified Fe 3 O 4 @C composite material with a mass ratio of 0.02gLa 3+ :Fe 3 O 4 @C is 2:1 is used for adsorption. The adsorption conditions were a temperature of 298K and a rotation speed of 200rpm with constant temperature shaking for 24h.
反应结束后,用钼酸铵分光光度法进行分析,结果表明,磷酸盐的吸附量为69.30mg-P/g。After the reaction, the ammonium molybdate spectrophotometric method was used for analysis. The results showed that the adsorption capacity of phosphate was 69.30mg-P/g.
实施例4Example 4
该实施例的碳酸镧改性Fe3O4@C复合材料制备方法同实施例2The preparation method of the lanthanum carbonate modified Fe 3 O 4 @C composite material in this example is the same as that in Example 2
吸附剂活性测试:Adsorbent activity test:
向一100ml锥形瓶中,加入50ml,浓度为50mg-P/L,pH=4.0±0.1的KH2PO4溶液。用0.02gLa3+:Fe3O4@C质量比为1:1的碳酸镧改性Fe3O4@C复合材料进行吸附。吸附条件为298K的温度、200rpm的转速下恒温振荡24h。To a 100 ml Erlenmeyer flask, add 50 ml of KH 2 PO 4 solution with a concentration of 50 mg-P/L and pH=4.0±0.1. The lanthanum carbonate-modified Fe 3 O 4 @C composite material with a mass ratio of 0.02gLa 3+ :Fe 3 O 4 @C is 1:1 was used for adsorption. The adsorption conditions were a temperature of 298K and a rotation speed of 200rpm with constant temperature shaking for 24h.
反应结束后,用钼酸铵分光光度法进行分析,结果表明,磷酸盐的吸附量为74.25mg-P/g。After the reaction, the ammonium molybdate spectrophotometric method was used for analysis. The results showed that the adsorption capacity of phosphate was 74.25mg-P/g.
对比例1Comparative example 1
Fe3O4@C复合材料,该对比例的材料制备方法与上述实施例2对应材料的区别是没有步骤(3)的碳酸镧改性。Fe 3 O 4 @C composite material, the difference between the material preparation method of this comparative example and the corresponding material of Example 2 above is that there is no lanthanum carbonate modification in step (3).
吸附剂活性测试:Adsorbent activity test:
向一100ml锥形瓶中,加入50ml,浓度为50mg-P/L,pH=7.0±0.1的KH2PO4溶液。用0.02gFe3O4@C复合材料进行吸附。吸附条件为298K的温度、200rpm的转速下恒温振荡24h。To a 100 ml Erlenmeyer flask, add 50 ml of KH 2 PO 4 solution with a concentration of 50 mg-P/L and pH=7.0±0.1. 0.02gFe 3 O 4 @C composite material was used for adsorption. The adsorption conditions were a temperature of 298K and a rotation speed of 200rpm with constant temperature shaking for 24h.
反应结束后,用钼酸铵分光光度法进行分析,结果表明,磷酸盐的吸附量为9.125mg-P/g。After the reaction, the ammonium molybdate spectrophotometric method was used for analysis. The results showed that the adsorption capacity of phosphate was 9.125mg-P/g.
对比例2Comparative example 2
纯碳酸镧的制备方法,包括以下步骤:The preparation method of pure lanthanum carbonate includes the following steps:
将1.486gLaCl3·7H2O超声溶解在50ml去离子水后,边快速机械搅拌,边以0.4ml/min的速度滴加1mol/LNaHCO3溶液,直至pH为中性,静置一晚。磁分离后固体用去离子水洗涤三次,60℃下干燥12h。After ultrasonically dissolving 1.486g LaCl 3 ·7H 2 O in 50ml deionized water, add 1mol/L NaHCO 3 solution dropwise at a speed of 0.4ml/min with rapid mechanical stirring until the pH is neutral, and let it stand overnight. After magnetic separation, the solid was washed three times with deionized water and dried at 60°C for 12 h.
吸附剂活性测试:Adsorbent activity test:
向一100ml锥形瓶中,加入50ml,浓度为50mg-P/L,pH=7.0±0.1的KH2PO4溶液。用0.02g纯碳酸镧进行吸附。吸附条件为298K的温度、200rpm的转速下恒温振荡24h。To a 100 ml Erlenmeyer flask, add 50 ml of KH 2 PO 4 solution with a concentration of 50 mg-P/L and pH=7.0±0.1. Use 0.02g of pure lanthanum carbonate for adsorption. The adsorption conditions were a temperature of 298K and a rotation speed of 200rpm with constant temperature shaking for 24h.
反应结束后,以钼酸铵分光光度法分析,结果表明,该材料磷酸盐吸附量为47.13mg-P/g。After the reaction, the ammonium molybdate spectrophotometric method was used to analyze the material. The results showed that the phosphate adsorption capacity of the material was 47.13mg-P/g.
对比例3Comparative example 3
La3+:Fe3O4@C质量比为1:1的氢氧化镧改性Fe3O4@C复合材料制备方法,包括以下步骤:A method for preparing a lanthanum hydroxide-modified Fe 3 O 4 @C composite material with a La 3+ : Fe 3 O 4 @C mass ratio of 1:1, including the following steps:
步骤(1)、(2)同实施例2。Steps (1) and (2) are the same as in Example 2.
步骤(3)将1.486gLaCl3·7H2O超声溶解在50ml去离子水中,加入0.556g步骤(2)制得的Fe3O4@C,在恒温振荡器中振荡搅拌4h。边快速机械搅拌,边以0.4ml/min的速度往上述悬浊液中滴加1mol/L NaOH溶液,直至pH为11±0.1,静置一晚。磁分离后固体用去离子水洗涤三次,60℃下干燥12h。Step (3) Ultrasonically dissolve 1.486g LaCl 3 ·7H 2 O in 50 ml deionized water, add 0.556g Fe 3 O 4 @C prepared in step (2), and oscillate and stir in a constant temperature oscillator for 4 hours. While rapidly mechanically stirring, add 1 mol/L NaOH solution dropwise to the above suspension at a speed of 0.4 ml/min until the pH is 11±0.1, and let it stand overnight. After magnetic separation, the solid was washed three times with deionized water and dried at 60°C for 12 h.
吸附剂活性测试:Adsorbent activity test:
向一100ml锥形瓶中,加入50ml,浓度为50mg-P/L,pH=7.0±0.1的KH2PO4溶液。用0.02gLa3+:Fe3O4@C质量比为1:1的氢氧化镧改性Fe3O4@C复合材料进行吸附。吸附条件为298K的温度、200rpm的转速下恒温振荡24h。To a 100 ml Erlenmeyer flask, add 50 ml of KH 2 PO 4 solution with a concentration of 50 mg-P/L and pH=7.0±0.1. The lanthanum hydroxide-modified Fe 3 O 4 @C composite material with a mass ratio of 0.02gLa 3+ :Fe 3 O 4 @C is 1:1 was used for adsorption. The adsorption conditions were a temperature of 298K and a rotation speed of 200rpm with constant temperature shaking for 24h.
反应结束后,用钼酸铵分光光度法进行分析,结果表明,磷酸盐的吸附量为36.98mg-P/g。After the reaction, the ammonium molybdate spectrophotometric method was used for analysis. The results showed that the adsorption capacity of phosphate was 36.98mg-P/g.
实施例1-4以及对比例1-3中吸附剂对磷酸盐的吸附性能对比图如图1所示,实施例1~3是按不同质量比例制备的碳酸镧改性Fe3O4@C复合材料在模拟中性条件下的吸附示例;实施例4是在模拟酸性条件下的吸附示例。可以看出,不管含磷模拟废水是酸性或是中性条件,本发明的吸附剂都有很好的吸附容量。The comparison chart of the adsorption performance of the adsorbents for phosphate in Examples 1-4 and Comparative Examples 1-3 is shown in Figure 1. Examples 1-3 are lanthanum carbonate-modified Fe 3 O 4 @C prepared at different mass ratios. Examples of adsorption of composite materials under simulated neutral conditions; Example 4 is an example of adsorption under simulated acidic conditions. It can be seen that the adsorbent of the present invention has good adsorption capacity regardless of whether the phosphorus-containing simulated wastewater is in acidic or neutral conditions.
对比例1~3是与实施例2进行对比的。对比例1说明Fe3O4@C基底自身吸附容量极小;对比例2比实施例2吸附量少,说明Fe3O4@C基底有助于活性物质碳酸镧的分散;对比例3比实施例2吸附量少,说明利用碳酸镧改性比利用氢氧化镧改性更为优越。Comparative Examples 1 to 3 are compared with Example 2. Comparative Example 1 shows that the Fe 3 O 4 @C substrate has extremely small self-adsorption capacity; Comparative Example 2 has less adsorption capacity than Example 2, indicating that the Fe 3 O 4 @C substrate contributes to the dispersion of the active material lanthanum carbonate; Comparative Example 3 is more The amount of adsorption in Example 2 is small, indicating that modification with lanthanum carbonate is more superior than modification with lanthanum hydroxide.
实施例2中对应材料的等温吸附线图(吸附剂投加量为0.4g/L,溶液初始pH=7±0.1,吸附温度为298K)如图2所示,从图2中可以本发明制备的碳酸镧改性Fe3O4@C复合材料具有很高的吸附容量,本发明的吸附剂对磷酸盐的吸附更符合Langmuir模型,该模型计算得到在吸附剂投加量为0.4g/L,溶液pH=7±0.1,吸附温度为298K的吸附条件下最大理论吸附量可达74.63mg-P/g。The isothermal adsorption diagram of the corresponding material in Example 2 (adsorbent dosage is 0.4g/L, initial solution pH=7±0.1, adsorption temperature is 298K) is shown in Figure 2. From Figure 2, it can be prepared by the present invention The lanthanum carbonate-modified Fe 3 O 4 @C composite material has a high adsorption capacity. The adsorption of phosphate by the adsorbent of the present invention is more consistent with the Langmuir model. The model calculates that the adsorbent dosage is 0.4g/L. , solution pH=7±0.1, and the maximum theoretical adsorption capacity can reach 74.63mg-P/g under the adsorption conditions of adsorption temperature of 298K.
实施例2中对应材料在不同初始pH下的吸附量图(吸附剂投加量为0.4g/L,溶液初始浓度为50mg-P/L,吸附温度为298K)如图3所示,从图3中可以看出,本发明制备的碳酸镧改性Fe3O4@C复合材料在酸性或中性的条件下有很好的吸附性能。The adsorption capacity diagram of the corresponding material in Example 2 at different initial pH (adsorbent dosage is 0.4g/L, initial solution concentration is 50mg-P/L, adsorption temperature is 298K) is shown in Figure 3. From Figure It can be seen from 3 that the lanthanum carbonate modified Fe 3 O 4 @C composite material prepared by the present invention has good adsorption performance under acidic or neutral conditions.
实施例2中对应材料的磁性分离图如图4所示,从图4可以看出本发明制备的碳酸镧改性Fe3O4@C复合材料具有强磁性,可以方便地进行固液分离操作。The magnetic separation diagram of the corresponding material in Example 2 is shown in Figure 4. It can be seen from Figure 4 that the lanthanum carbonate-modified Fe3O4@C composite material prepared by the present invention has strong magnetism and can easily perform solid-liquid separation operations.
将实施例2与对比例1和2进行对比可知,当用等量的吸附剂时,碳酸镧改性Fe3O4@C复合材料比单独的碳酸镧以及单独的Fe3O4@C的吸附效果都要好,说明碳酸镧和Fe3O4@C产生了协同作用。Comparing Example 2 with Comparative Examples 1 and 2, it can be seen that when the same amount of adsorbent is used, the lanthanum carbonate-modified Fe 3 O 4 @C composite material is better than the lanthanum carbonate alone and the Fe 3 O 4 @C alone. The adsorption effects are all good, indicating that lanthanum carbonate and Fe 3 O 4 @C have a synergistic effect.
上述实施例为本发明较佳的实施方式,但本发明的实施方式并不受上述实施例的限制,其他的任何未背离本发明的精神实质与原理下所作的改变、修饰、替代、组合、简化,均应为等效的置换方式,都包含在本发明的保护范围之内。The above embodiments are preferred embodiments of the present invention, but the embodiments of the present invention are not limited to the above embodiments. Any other changes, modifications, substitutions, combinations, etc. may be made without departing from the spirit and principles of the present invention. All simplifications should be equivalent substitutions, and are all included in the protection scope of the present invention.
Claims (10)
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202110213537.6A CN114950352B (en) | 2021-02-26 | 2021-02-26 | Lanthanum carbonate modified Fe 3 O 4 Dephosphorization adsorbent at@C and preparation method and application thereof |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202110213537.6A CN114950352B (en) | 2021-02-26 | 2021-02-26 | Lanthanum carbonate modified Fe 3 O 4 Dephosphorization adsorbent at@C and preparation method and application thereof |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN114950352A CN114950352A (en) | 2022-08-30 |
| CN114950352B true CN114950352B (en) | 2023-11-10 |
Family
ID=82973141
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202110213537.6A Active CN114950352B (en) | 2021-02-26 | 2021-02-26 | Lanthanum carbonate modified Fe 3 O 4 Dephosphorization adsorbent at@C and preparation method and application thereof |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN114950352B (en) |
Families Citing this family (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN117380147A (en) * | 2023-10-31 | 2024-01-12 | 江西理工大学 | A magnetic adsorbent for adsorbing rare earth ions and its preparation method and application |
| CN117582937A (en) * | 2024-01-08 | 2024-02-23 | 北京林业大学 | Efficient dephosphorization environment adsorption material lanthanum hydroxide and synthesis method thereof |
Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103406108A (en) * | 2013-07-10 | 2013-11-27 | 江苏大学 | Preparation method of carbon-based magnetic temperature-sensitive surface imprinted adsorbent |
| CN103906523A (en) * | 2011-09-08 | 2014-07-02 | 柏林夏洛蒂医科大学 | Nanoparticle phosphate adsorbents based on maghemite or maghemite/magnetite, their preparation and use |
| CN109569552A (en) * | 2018-12-13 | 2019-04-05 | 北京林业大学 | A kind of magnetic/non magnetic lanthanum carbonate sodium dephosphorization adsorbent and its synthetic method |
| CN110652963A (en) * | 2019-11-01 | 2020-01-07 | 广州大学 | A kind of lanthanum carbonate modified co-pyrolysis sludge biochar and its preparation method and application |
-
2021
- 2021-02-26 CN CN202110213537.6A patent/CN114950352B/en active Active
Patent Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103906523A (en) * | 2011-09-08 | 2014-07-02 | 柏林夏洛蒂医科大学 | Nanoparticle phosphate adsorbents based on maghemite or maghemite/magnetite, their preparation and use |
| CN103406108A (en) * | 2013-07-10 | 2013-11-27 | 江苏大学 | Preparation method of carbon-based magnetic temperature-sensitive surface imprinted adsorbent |
| CN109569552A (en) * | 2018-12-13 | 2019-04-05 | 北京林业大学 | A kind of magnetic/non magnetic lanthanum carbonate sodium dephosphorization adsorbent and its synthetic method |
| CN110652963A (en) * | 2019-11-01 | 2020-01-07 | 广州大学 | A kind of lanthanum carbonate modified co-pyrolysis sludge biochar and its preparation method and application |
Also Published As
| Publication number | Publication date |
|---|---|
| CN114950352A (en) | 2022-08-30 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN105688825B (en) | A kind of magnetic adsorbent preparation method and application based on ferrous metals organic framework material | |
| CN107999033B (en) | A polydopamine/aminated carbon nanotube/sodium alginate microsphere for adsorbing arsenic | |
| CN104353406B (en) | A kind of double-metal hydroxide and preparation method thereof, magnetic dephosphorization adsorbent and preparation method thereof | |
| CN109569725B (en) | A one-step method for preparing magnetic Cu(I) microsphere catalyst | |
| CN102258980B (en) | Method for preparing sulfured magnetic chitosan and method for treating waste water containing heavy metals by using sulfured magnetic chitosan | |
| CN103102002B (en) | Application of Pd/Fe3O4 catalyst for removal of nitrate or nitrite in aqueous solution | |
| CN114950352B (en) | Lanthanum carbonate modified Fe 3 O 4 Dephosphorization adsorbent at@C and preparation method and application thereof | |
| CN104826600B (en) | A kind of magnetic kleit preparation method | |
| CN104891513B (en) | A kind of preparation method of magnetic bentonite | |
| CN109939649A (en) | A kind of preparation method of magnetic chitosan-sodium alginate gel ball | |
| CN102553528B (en) | A modified carbon nanotube material, a method for removing mercury ions in water and a regeneration method thereof | |
| CN108212072A (en) | It is a kind of to be applied for the adsorbent of cesium ion removal in water and its in Cs absorption | |
| CN111229167A (en) | Thiosemicarbazide modified magnetic graphene oxide adsorbent and preparation method and application thereof | |
| CN108640262B (en) | Magnetic nano-chitosan microspheres and preparation method thereof | |
| Yang et al. | Recyclable hydrogel-MOFs composite beads for selective removal of Pb (II) from water | |
| CN111939911A (en) | Preparation method and application of β-FeOOH/SiO2 composite catalyst | |
| CN115106071A (en) | Novel magnetic material for sewage treatment and application thereof | |
| CN107469797B (en) | A kind of preparation method of dimercaptosuccinic acid modified porous magnetic composite microsphere | |
| CN110586045A (en) | Preparation method and application of amphoteric magnetic chitosan adsorbent | |
| CN110721654A (en) | Magnetic crystal/amorphous lanthanum zirconium iron oxide phosphorus removal adsorbent and synthesis method thereof | |
| CN110124640A (en) | The application of the compound and preparation and adsorption and dephosphorization of lanthanum molybdate and ferrimagnet | |
| CN102826607A (en) | Mesoporous zinc ferrite, preparation method thereof, and magnetic carbon nanotube prepared from same | |
| CN114405475A (en) | Adsorbing material and preparation method and application thereof | |
| CN116809034B (en) | Preparation method of phosphorus removal agent based on rare earth modified coal gangue | |
| CN106378111B (en) | A kind of magnetic Fe with nucleocapsid3O4/ PMMA nano-compound adsorbents and preparation method thereof |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| PB01 | Publication | ||
| PB01 | Publication | ||
| SE01 | Entry into force of request for substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| GR01 | Patent grant | ||
| GR01 | Patent grant |