CN106000324A - Preparation method of magnetic organic hydrotalcite - Google Patents
Preparation method of magnetic organic hydrotalcite Download PDFInfo
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- CN106000324A CN106000324A CN201610405865.5A CN201610405865A CN106000324A CN 106000324 A CN106000324 A CN 106000324A CN 201610405865 A CN201610405865 A CN 201610405865A CN 106000324 A CN106000324 A CN 106000324A
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- GDVKFRBCXAPAQJ-UHFFFAOYSA-A dialuminum;hexamagnesium;carbonate;hexadecahydroxide Chemical compound [OH-].[OH-].[OH-].[OH-].[OH-].[OH-].[OH-].[OH-].[OH-].[OH-].[OH-].[OH-].[OH-].[OH-].[OH-].[OH-].[Mg+2].[Mg+2].[Mg+2].[Mg+2].[Mg+2].[Mg+2].[Al+3].[Al+3].[O-]C([O-])=O GDVKFRBCXAPAQJ-UHFFFAOYSA-A 0.000 title claims abstract description 21
- 229960001545 hydrotalcite Drugs 0.000 title claims abstract description 20
- 229910001701 hydrotalcite Inorganic materials 0.000 title claims abstract description 20
- 238000002360 preparation method Methods 0.000 title claims abstract description 7
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 29
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 claims abstract description 18
- MHAJPDPJQMAIIY-UHFFFAOYSA-N Hydrogen peroxide Chemical compound OO MHAJPDPJQMAIIY-UHFFFAOYSA-N 0.000 claims abstract description 14
- 239000002244 precipitate Substances 0.000 claims abstract description 11
- 239000007788 liquid Substances 0.000 claims abstract description 9
- 238000000034 method Methods 0.000 claims abstract description 7
- 238000000926 separation method Methods 0.000 claims abstract description 7
- 239000004094 surface-active agent Substances 0.000 claims abstract description 7
- 230000008569 process Effects 0.000 claims abstract description 6
- 239000007787 solid Substances 0.000 claims abstract description 6
- 238000001035 drying Methods 0.000 claims description 5
- 229910021577 Iron(II) chloride Inorganic materials 0.000 claims description 4
- -1 alkyl carbon 12 Chemical compound 0.000 claims description 4
- 238000001556 precipitation Methods 0.000 claims 2
- 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
- 150000008052 alkyl sulfonates Chemical class 0.000 claims 1
- 238000002242 deionisation method Methods 0.000 claims 1
- 229910052708 sodium Inorganic materials 0.000 claims 1
- 239000011734 sodium Substances 0.000 claims 1
- JHJUUEHSAZXEEO-UHFFFAOYSA-M sodium;4-dodecylbenzenesulfonate Chemical compound [Na+].CCCCCCCCCCCCC1=CC=C(S([O-])(=O)=O)C=C1 JHJUUEHSAZXEEO-UHFFFAOYSA-M 0.000 claims 1
- 238000003756 stirring Methods 0.000 abstract description 8
- 238000001179 sorption measurement Methods 0.000 abstract description 7
- 239000008367 deionised water Substances 0.000 abstract description 4
- 229910021641 deionized water Inorganic materials 0.000 abstract description 4
- 230000009286 beneficial effect Effects 0.000 abstract 1
- 239000003344 environmental pollutant Substances 0.000 abstract 1
- 231100000719 pollutant Toxicity 0.000 abstract 1
- 239000011229 interlayer Substances 0.000 description 6
- 150000001450 anions Chemical class 0.000 description 5
- 150000001768 cations Chemical class 0.000 description 5
- 150000001875 compounds Chemical class 0.000 description 4
- 239000000463 material Substances 0.000 description 4
- 238000005406 washing Methods 0.000 description 4
- 238000006243 chemical reaction Methods 0.000 description 3
- GVGUFUZHNYFZLC-UHFFFAOYSA-N dodecyl benzenesulfonate;sodium Chemical compound [Na].CCCCCCCCCCCCOS(=O)(=O)C1=CC=CC=C1 GVGUFUZHNYFZLC-UHFFFAOYSA-N 0.000 description 3
- XEEYBQQBJWHFJM-UHFFFAOYSA-N iron Substances [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 3
- NMCUIPGRVMDVDB-UHFFFAOYSA-L iron dichloride Chemical compound Cl[Fe]Cl NMCUIPGRVMDVDB-UHFFFAOYSA-L 0.000 description 3
- 239000002184 metal Substances 0.000 description 3
- 229910052751 metal Inorganic materials 0.000 description 3
- 229940080264 sodium dodecylbenzenesulfonate Drugs 0.000 description 3
- 239000000126 substance Substances 0.000 description 3
- 239000006228 supernatant Substances 0.000 description 3
- BTJIUGUIPKRLHP-UHFFFAOYSA-N 4-nitrophenol Chemical compound OC1=CC=C([N+]([O-])=O)C=C1 BTJIUGUIPKRLHP-UHFFFAOYSA-N 0.000 description 2
- UQSXHKLRYXJYBZ-UHFFFAOYSA-N Iron oxide Chemical compound [Fe]=O UQSXHKLRYXJYBZ-UHFFFAOYSA-N 0.000 description 2
- 239000004927 clay Substances 0.000 description 2
- 230000007613 environmental effect Effects 0.000 description 2
- 150000002500 ions Chemical class 0.000 description 2
- 239000010410 layer Substances 0.000 description 2
- 230000004048 modification Effects 0.000 description 2
- 238000012986 modification Methods 0.000 description 2
- 239000012044 organic layer Substances 0.000 description 2
- 239000002957 persistent organic pollutant Substances 0.000 description 2
- 239000011148 porous material Substances 0.000 description 2
- PNGBYKXZVCIZRN-UHFFFAOYSA-M sodium;hexadecane-1-sulfonate Chemical compound [Na+].CCCCCCCCCCCCCCCCS([O-])(=O)=O PNGBYKXZVCIZRN-UHFFFAOYSA-M 0.000 description 2
- VTLYFUHAOXGGBS-UHFFFAOYSA-N Fe3+ Chemical compound [Fe+3] VTLYFUHAOXGGBS-UHFFFAOYSA-N 0.000 description 1
- 229910019440 Mg(OH) Inorganic materials 0.000 description 1
- 230000009471 action Effects 0.000 description 1
- 239000003513 alkali Substances 0.000 description 1
- 125000005227 alkyl sulfonate group Chemical group 0.000 description 1
- 150000001449 anionic compounds Chemical class 0.000 description 1
- 230000008901 benefit Effects 0.000 description 1
- 229910052599 brucite Inorganic materials 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 150000001767 cationic compounds Chemical class 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 238000000975 co-precipitation Methods 0.000 description 1
- 239000002131 composite material Substances 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000003933 environmental pollution control Methods 0.000 description 1
- 125000005842 heteroatom Chemical group 0.000 description 1
- 230000002209 hydrophobic effect Effects 0.000 description 1
- 229910001412 inorganic anion Inorganic materials 0.000 description 1
- 229910001411 inorganic cation Inorganic materials 0.000 description 1
- 238000005342 ion exchange Methods 0.000 description 1
- 229910052742 iron Inorganic materials 0.000 description 1
- JEIPFZHSYJVQDO-UHFFFAOYSA-N iron(III) oxide Inorganic materials O=[Fe]O[Fe]=O JEIPFZHSYJVQDO-UHFFFAOYSA-N 0.000 description 1
- 230000007935 neutral effect Effects 0.000 description 1
- LQNUZADURLCDLV-UHFFFAOYSA-N nitrobenzene Chemical compound [O-][N+](=O)C1=CC=CC=C1 LQNUZADURLCDLV-UHFFFAOYSA-N 0.000 description 1
- 150000002891 organic anions Chemical class 0.000 description 1
- 150000002892 organic cations Chemical class 0.000 description 1
- 229920000447 polyanionic polymer Polymers 0.000 description 1
- 239000000454 talc Substances 0.000 description 1
- 229910052623 talc Inorganic materials 0.000 description 1
- 230000009466 transformation Effects 0.000 description 1
Classifications
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- 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
- B01J20/22—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising organic material
-
- 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
- B01J20/28—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
-
- 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
- B01J2220/00—Aspects relating to sorbent materials
- B01J2220/40—Aspects relating to the composition of sorbent or filter aid materials
- B01J2220/46—Materials comprising a mixture of inorganic and organic materials
-
- 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
- B01J2220/00—Aspects relating to sorbent materials
- B01J2220/40—Aspects relating to the composition of sorbent or filter aid materials
- B01J2220/48—Sorbents characterised by the starting material used for their preparation
- B01J2220/4806—Sorbents characterised by the starting material used for their preparation the starting material being of inorganic character
-
- 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
- B01J2220/00—Aspects relating to sorbent materials
- B01J2220/40—Aspects relating to the composition of sorbent or filter aid materials
- B01J2220/48—Sorbents characterised by the starting material used for their preparation
- B01J2220/4812—Sorbents characterised by the starting material used for their preparation the starting material being of organic character
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- Chemical & Material Sciences (AREA)
- Analytical Chemistry (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Inorganic Chemistry (AREA)
- Solid-Sorbent Or Filter-Aiding Compositions (AREA)
- Compounds Of Iron (AREA)
Abstract
本发明公开一种磁性有机水滑石的制备方法。依次包括如下步骤:取FeCl2该溶液,将其中置于恒温70~80℃水浴中,同时滴加30%(质量分数)双氧水2~4mL和一定量的NaOH稀溶液,保持pH值为12~13,反应2~3h,转入高压釜中,在1h内升温到150~180℃,继续反应4~8h,自然冷却到室温,在该过程中形成具有层状结构的沉淀,沉淀分离,去离子水洗2~3遍;将沉淀得到的固体加入到浓度为2~4mol/L的表面活性剂溶液中,固液比为1:10~1:50,在50~80℃水浴中搅拌2~8h,磁场分离后用去离子水洗涤2~3遍,70~90℃烘干,即可得到一种磁性有机水滑石。该结构有利于吸附污染物,同时有利于分离。The invention discloses a preparation method of magnetic organic hydrotalcite. Include the following steps in sequence: take the FeCl solution, place it in a water bath with a constant temperature of 70-80°C, and simultaneously add 2-4mL of 30% (mass fraction) hydrogen peroxide and a certain amount of dilute NaOH solution dropwise, keeping the pH value at 12-80°C. 13. React for 2-3 hours, transfer to an autoclave, heat up to 150-180°C within 1 hour, continue to react for 4-8 hours, and cool down to room temperature naturally. During this process, a precipitate with a layered structure is formed, and the precipitate is separated and removed. Wash 2 to 3 times with ionized water; add the precipitated solid to a surfactant solution with a concentration of 2 to 4 mol/L, the solid-to-liquid ratio is 1:10 to 1:50, and stir in a water bath at 50 to 80°C for 2 to After 8 hours of magnetic field separation, wash with deionized water for 2 to 3 times, and dry at 70 to 90°C to obtain a magnetic organic hydrotalcite. This structure is beneficial for the adsorption of pollutants and at the same time for separation.
Description
技术领域technical field
本发明涉及环境污染控制新材料的开发,尤其涉及一种磁性有机水滑石的制备方法。The invention relates to the development of new materials for environmental pollution control, in particular to a preparation method of magnetic organic hydrotalcite.
背景技术Background technique
水滑石类化合物(LDHs)是由层间阴离子及带正电荷层板堆积而成的化合物。水滑石化学结构通式为:[M2+ 1-xM3+x(OH)2]x+[(An-)x/n·mH2O],其中M2+和M3+分别为位于主体层板上的二价和三价金属阳离子,如Mg2+、Ni2+、Zn2+、Mn2+、Cu2+、Co2+、Pd2+、Fe2+等二价阳离子和Al3+、Cr3+、Co3+、Fe3+等三价阳离子均可以形成水滑石;An–为层间阴离子,可以包括无机阴离子,有机阴离子,配合物阴离子、同多和杂多阴离子;x为M3+/(M2++M3+)的摩尔比值,大约是4:1到2:1;m为层间水分子的个数。其结构类似于水镁石Mg(OH)2,由八面体共用棱边而形成主体层板。位于层板上的二价金属阳离子M2+可以在一定的比例范围内被离子半价相近的三价金属阳离子M3+同晶取代,使得层板带正电荷,层间存在可以交换的的阴离子与层板上的正电荷平衡,使得LDHs的整体结构呈电中性。层间的阴离子可被交换,经过一系列改性,水滑石材料可以得到许多种性能各异的物质。Hydrotalcite-like compounds (LDHs) are compounds formed by stacking interlayer anions and positively charged laminates. The general chemical structure formula of hydrotalcite is: [M 2+ 1-x M 3+ x(OH) 2 ] x+ [(A n- ) x/n mH 2 O], where M 2+ and M 3+ are respectively Divalent and trivalent metal cations located on the main laminate, such as Mg 2+ , Ni 2+ , Zn 2+ , Mn 2+ , Cu 2+ , Co 2+ , Pd 2+ , Fe 2+ and other divalent cations Al 3+ , Cr 3+ , Co 3+ , Fe 3+ and other trivalent cations can form hydrotalcite; An– is an interlayer anion, which can include inorganic anions, organic anions, complex anions, isopoly and hetero Polyanions; x is the molar ratio of M 3+ /(M 2+ +M 3+ ), about 4:1 to 2:1; m is the number of interlayer water molecules. Its structure is similar to that of brucite Mg(OH) 2 , and the main laminates are formed by octahedrons sharing edges. The divalent metal cation M 2+ located on the laminate can be isomorphically replaced by the trivalent metal cation M 3+ with a similar half price within a certain proportion, so that the laminate is positively charged and there are exchangeable anions between the layers Balanced with the positive charge on the laminate, the overall structure of LDHs is electrically neutral. The anions between the layers can be exchanged, and after a series of modifications, the hydrotalcite material can obtain many kinds of substances with different properties.
通过离子交换等方式把一些化合物引入层间域,形成分子级别的支柱,制成的一类孔径大、分布规则的新型分子水平复合材料,具有吸附、转化有机分子的特点。水滑石品种多,支柱化合物的可调性,改性后的粘土材料孔径大小、吸附性质等可以人为加以控制,因此可以根据用途的不同来进行材料制备,在石油化工、环境保护等诸多领域有广泛应用前景。Some compounds are introduced into the interlayer domain by means of ion exchange to form molecular-level pillars, and a new type of molecular-level composite material with large pore size and regular distribution is produced, which has the characteristics of adsorption and transformation of organic molecules. There are many varieties of hydrotalcite, the adjustability of the pillar compound, the pore size and adsorption properties of the modified clay material can be controlled artificially, so the material can be prepared according to different uses, and it is widely used in petrochemical, environmental protection and many other fields Wide application prospects.
最普遍的方式就是通过改性得到有机层状粘土加以应用,即将层间无机阳离子经过有机阳离子(通常为季铵盐阳离子)交换后,生成有机层状物,层间和外表面的疏水性提高,因而可以更加有效地吸附去除有机污染物。由于有机层状物的这种优异吸附性能,使其在环境保护领域有广泛的应用潜力。经过有机化改性后的水滑石由于对部分亲水性强的有机物有较好的吸附效果。但吸附后存在分离困难的问题,如果要分离干净,需要经过多个步骤,费时费力。The most common way is to obtain organic layered clay by modification, that is, after the interlayer inorganic cations are exchanged with organic cations (usually quaternary ammonium salt cations), an organic layer is formed, and the hydrophobicity of the interlayer and the outer surface is improved. , so that organic pollutants can be more effectively adsorbed and removed. Due to the excellent adsorption properties of the organic layer, it has a wide application potential in the field of environmental protection. The organically modified hydrotalcite has a better adsorption effect on some organic substances with strong hydrophilicity. However, there is the problem of difficult separation after adsorption. If it is to be separated cleanly, it needs to go through multiple steps, which is time-consuming and laborious.
发明内容Contents of the invention
本发明的目的是为克服现有技术中氧化铁结构单一的不足,提供一种磁性有机水滑石的制备方法。The object of the present invention is to provide a preparation method of magnetic organic hydrotalcite to overcome the deficiency of single structure of iron oxide in the prior art.
本发明采用的技术方案是依次包括如下步骤:The technical scheme that the present invention adopts is to comprise the following steps successively:
1)将FeCl2溶解到水中,配置为浓度为2~3mol/L的溶液,取500mL该溶液,将其中置于恒温70~80℃水浴中,同时滴加30%(质量分数)双氧水2~4mL和一定量的NaOH稀溶液,保持pH值为12~13,反应2~3h,转入高压釜中,在1h内升温到150~180℃,继续反应4~8h,自然冷却到室温,在该过程中形成具有层状结构的沉淀,沉淀分离,去离子水洗2~3遍;1) Dissolve FeCl 2 in water and prepare a solution with a concentration of 2-3mol/L. Take 500mL of the solution, place it in a water bath with a constant temperature of 70-80°C, and add 30% (mass fraction) hydrogen peroxide dropwise at the same time. 4mL and a certain amount of dilute NaOH solution, keep the pH value at 12~13, react for 2~3h, transfer to an autoclave, heat up to 150~180°C within 1h, continue to react for 4~8h, cool naturally to room temperature, During this process, a precipitate with a layered structure is formed, the precipitate is separated, and washed 2 to 3 times with deionized water;
2)将沉淀得到的固体加入到浓度为2~4mol/L的表面活性剂溶液中,固液比为1:10~1:50,在50~80℃水浴中搅拌2~8h,磁场分离后用去离子水洗涤2~3遍,70~90℃烘干,即可得到一种磁性有机水滑石。2) Add the precipitated solid into a surfactant solution with a concentration of 2-4mol/L, the solid-to-liquid ratio is 1:10-1:50, stir in a water bath at 50-80°C for 2-8 hours, and after magnetic field separation Washing with deionized water for 2 to 3 times and drying at 70 to 90 DEG C can obtain a magnetic organic hydrotalcite.
表面活性剂是烷基碳数在12或12以上的烷基磺酸盐,如十二烷基苯磺酸钠、十六烷基磺酸钠等。The surfactant is an alkyl sulfonate with an alkyl carbon number of 12 or more, such as sodium dodecylbenzenesulfonate, sodium cetylsulfonate, etc.
本发明的优点是:部分二价铁离子被双氧水氧化生成的三价铁,二价离子和生成的三价离子在70~80℃水浴中碱的作用下,产生磁性共沉淀,形成片层水滑石结构,再在片层间交换入表面活性剂,使其表面由疏水性转变为亲水性,该结构有利于吸附去除有机污染物,去除之后有利于分离。The advantage of the present invention is that part of the divalent iron ions are oxidized by hydrogen peroxide to produce ferric iron, and the divalent ions and the generated trivalent ions will produce magnetic co-precipitation under the action of alkali in a water bath at 70-80°C to form lamellar water. Talc structure, and then exchange surfactants between the sheets to make the surface change from hydrophobic to hydrophilic. This structure is conducive to the adsorption and removal of organic pollutants, and is conducive to separation after removal.
具体实施方式detailed description
以下进一步提供本发明的3个实施例:Further provide 3 embodiments of the present invention below:
实施例1Example 1
将FeCl2溶解到水中,配置为浓度为3mol/L的溶液,取500mL该溶液,将其置于恒温80℃水浴中,同时滴加30%(质量分数)双氧水4mL和一定量的NaOH稀溶液,保持pH值为13,反应3h,转入高压釜中,在1h内升温到180℃,继续反应8h,自然冷却到室温,在该过程中形成具有层状结构的沉淀,沉淀分离,去离子水洗3遍;将沉淀得到的固体加入到浓度为4mol/L的十二烷基苯磺酸钠溶液中,固液比为1:50,在80℃水浴中搅拌8h,磁场分离后用去离子水洗涤3遍,90℃烘干,即可得到一种磁性有机水滑石。Dissolve FeCl2 in water and make a solution with a concentration of 3mol/L. Take 500mL of this solution and place it in a water bath with a constant temperature of 80°C. At the same time, add 4mL of 30% (mass fraction) hydrogen peroxide and a certain amount of NaOH dilute solution dropwise. , keep the pH value at 13, react for 3 hours, transfer to an autoclave, raise the temperature to 180°C within 1 hour, continue the reaction for 8 hours, and naturally cool to room temperature. During this process, a precipitate with a layered structure is formed, the precipitate is separated, and deionized Wash 3 times with water; add the precipitated solid to the sodium dodecylbenzenesulfonate solution with a concentration of 4 mol/L, the solid-to-liquid ratio is 1:50, stir in a water bath at 80°C for 8 hours, separate with a magnetic field and use a deionized After washing with water for three times and drying at 90°C, a magnetic organic hydrotalcite can be obtained.
将1g磁性有机水滑石加入到浓度为15mg/L、体积为1L的对硝基苯酚溶液中,搅拌2h,磁场分离,紫外可见分光光度计测定上清液浓度,去除率为92.2%,上清液可以排放。Add 1 g of magnetic organic hydrotalcite to a p-nitrophenol solution with a concentration of 15 mg/L and a volume of 1 L, stir for 2 hours, separate with a magnetic field, measure the concentration of the supernatant with a UV-visible spectrophotometer, and the removal rate is 92.2%. Liquid can be drained.
实施例2Example 2
将FeCl2溶解到水中,配置为浓度为2mol/L的溶液,取500mL该溶液,将其置于恒温70℃水浴中,同时滴加30%(质量分数)双氧水2mL和一定量的NaOH稀溶液,保持pH值为12,反应2h,转入高压釜中,在1h内升温到150℃,继续反应4h,自然冷却到室温,在该过程中形成具有层状结构的沉淀,沉淀分离,去离子水洗2遍;将沉淀得到的固体加入到浓度为2mol/L的十六烷基磺酸钠溶液中,固液比为1:10,在50℃水浴中搅拌2h,磁场分离后用去离子水洗涤2遍,70℃烘干,即可得到一种磁性有机水滑石。Dissolve FeCl2 in water and configure it as a solution with a concentration of 2mol/L. Take 500mL of this solution and place it in a water bath with a constant temperature of 70°C. At the same time, add 2mL of 30% (mass fraction) hydrogen peroxide and a certain amount of dilute NaOH solution dropwise. , keep the pH value at 12, react for 2 hours, transfer to an autoclave, raise the temperature to 150°C within 1 hour, continue the reaction for 4 hours, and naturally cool to room temperature. During the process, a precipitate with a layered structure is formed, the precipitate is separated, and deionized Wash 2 times with water; add the precipitated solid to the sodium hexadecylsulfonate solution with a concentration of 2mol/L, the solid-to-liquid ratio is 1:10, stir in a water bath at 50°C for 2h, separate with deionized water after magnetic field separation After washing twice and drying at 70°C, a magnetic organic hydrotalcite can be obtained.
将1g磁性有机水滑石加入到浓度为15mg/L、体积为1L的对硝基苯酚溶液中,搅拌2h,磁场分离,紫外可见分光光度计测定上清液浓度,去除率为95.4%,上清液可以排放。Add 1 g of magnetic organic hydrotalcite to a p-nitrophenol solution with a concentration of 15 mg/L and a volume of 1 L, stir for 2 h, separate with a magnetic field, measure the concentration of the supernatant with a UV-visible spectrophotometer, and the removal rate is 95.4%. Liquid can be drained.
实施例3Example 3
将FeCl2溶解到水中,配置为浓度为3mol/L的溶液,取500mL该溶液,将其置于恒温80℃水浴中,同时滴加30%(质量分数)双氧水3mL和一定量的NaOH稀溶液,保持pH值为13,反应3h,转入高压釜中,在1h内升温到160℃,继续反应5h,自然冷却到室温,在该过程中形成具有层状结构的沉淀,沉淀分离,去离子水洗3遍;将沉淀得到的固体加入到浓度为3mol/L的十二烷基苯磺酸钠溶液中,固液比为1:40,在80℃水浴中搅拌8h,磁场分离后用去离子水洗涤3遍,90℃烘干,即可得到一种磁性有机水滑石。Dissolve FeCl2 in water and configure it as a solution with a concentration of 3mol/L. Take 500mL of this solution and place it in a water bath with a constant temperature of 80°C. At the same time, add 3mL of 30% (mass fraction) hydrogen peroxide and a certain amount of NaOH dilute solution dropwise. , keep the pH value at 13, react for 3 hours, transfer to an autoclave, raise the temperature to 160°C within 1 hour, continue the reaction for 5 hours, and naturally cool to room temperature. During this process, a precipitate with a layered structure is formed, the precipitate is separated, and deionized Wash 3 times with water; add the precipitated solid to the sodium dodecylbenzenesulfonate solution with a concentration of 3mol/L, the solid-to-liquid ratio is 1:40, stir in a water bath at 80°C for 8h, and separate with a deionized After washing with water for three times and drying at 90°C, a magnetic organic hydrotalcite can be obtained.
将1g磁性有机水滑石加入到浓度为5mg/L、体积为1L的对硝基苯中,搅拌2h,磁场分离,紫外可见分光光度计测定上清液浓度,去除率为99.2%,上清液可以排放。Add 1 g of magnetic organic hydrotalcite to p-nitrobenzene with a concentration of 5 mg/L and a volume of 1 L, stir for 2 hours, separate in a magnetic field, measure the concentration of the supernatant with a UV-visible spectrophotometer, and the removal rate is 99.2%. can be discharged.
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| US6323367B1 (en) * | 2000-11-22 | 2001-11-27 | Council Of Scientific And Industrial Research | Process for the preparation of amine oxides |
| CN101780985A (en) * | 2010-01-26 | 2010-07-21 | 苏州科技学院 | Hydrotalcite-like compound used for raw water treatment |
| CN103769037A (en) * | 2014-02-27 | 2014-05-07 | 南京农业大学 | Preparation method of roasted ferro-manganese hydrotalcite and application of roasted ferro-manganese hydrotalcite in adsorption of arsenic-polluted wastewater |
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| US6323367B1 (en) * | 2000-11-22 | 2001-11-27 | Council Of Scientific And Industrial Research | Process for the preparation of amine oxides |
| CN101780985A (en) * | 2010-01-26 | 2010-07-21 | 苏州科技学院 | Hydrotalcite-like compound used for raw water treatment |
| CN103769037A (en) * | 2014-02-27 | 2014-05-07 | 南京农业大学 | Preparation method of roasted ferro-manganese hydrotalcite and application of roasted ferro-manganese hydrotalcite in adsorption of arsenic-polluted wastewater |
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