CN108912269B - A kind of polyimidazole ionic liquid-based copolymer and its preparation method and application - Google Patents
A kind of polyimidazole ionic liquid-based copolymer and its preparation method and application Download PDFInfo
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- 239000002608 ionic liquid Substances 0.000 title claims abstract description 58
- 229920001577 copolymer Polymers 0.000 title claims abstract description 37
- 238000002360 preparation method Methods 0.000 title claims abstract description 17
- RAXXELZNTBOGNW-UHFFFAOYSA-N imidazole Natural products C1=CNC=N1 RAXXELZNTBOGNW-UHFFFAOYSA-N 0.000 claims abstract description 54
- WEVYAHXRMPXWCK-UHFFFAOYSA-N Acetonitrile Chemical compound CC#N WEVYAHXRMPXWCK-UHFFFAOYSA-N 0.000 claims abstract description 51
- MYRTYDVEIRVNKP-UHFFFAOYSA-N 1,2-Divinylbenzene Chemical compound C=CC1=CC=CC=C1C=C MYRTYDVEIRVNKP-UHFFFAOYSA-N 0.000 claims abstract description 31
- 239000003463 adsorbent Substances 0.000 claims abstract description 25
- 229910052702 rhenium Inorganic materials 0.000 claims abstract description 18
- WUAPFZMCVAUBPE-UHFFFAOYSA-N rhenium atom Chemical compound [Re] WUAPFZMCVAUBPE-UHFFFAOYSA-N 0.000 claims abstract description 18
- OSSNTDFYBPYIEC-UHFFFAOYSA-N 1-ethenylimidazole Chemical compound C=CN1C=CN=C1 OSSNTDFYBPYIEC-UHFFFAOYSA-N 0.000 claims abstract description 11
- 239000011837 N,N-methylenebisacrylamide Substances 0.000 claims abstract description 10
- ZIUHHBKFKCYYJD-UHFFFAOYSA-N n,n'-methylenebisacrylamide Chemical compound C=CC(=O)NCNC(=O)C=C ZIUHHBKFKCYYJD-UHFFFAOYSA-N 0.000 claims abstract description 10
- USHAGKDGDHPEEY-UHFFFAOYSA-L potassium persulfate Chemical compound [K+].[K+].[O-]S(=O)(=O)OOS([O-])(=O)=O USHAGKDGDHPEEY-UHFFFAOYSA-L 0.000 claims abstract description 7
- 238000001816 cooling Methods 0.000 claims abstract description 6
- 238000005406 washing Methods 0.000 claims abstract description 5
- 238000000967 suction filtration Methods 0.000 claims abstract description 4
- 238000001291 vacuum drying Methods 0.000 claims abstract description 4
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical group Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 claims description 14
- 229910052751 metal Inorganic materials 0.000 claims description 10
- 239000002184 metal Substances 0.000 claims description 10
- 239000003480 eluent Substances 0.000 claims description 9
- 238000010526 radical polymerization reaction Methods 0.000 claims description 5
- KJDRSWPQXHESDQ-UHFFFAOYSA-N 1,4-dichlorobutane Chemical compound ClCCCCCl KJDRSWPQXHESDQ-UHFFFAOYSA-N 0.000 claims description 4
- 239000003431 cross linking reagent Substances 0.000 claims description 3
- 238000011084 recovery Methods 0.000 claims description 3
- 239000000178 monomer Substances 0.000 claims description 2
- QUBRHRAWRVZUFZ-UHFFFAOYSA-N 1,4-dichlorohexane Chemical compound CCC(Cl)CCCCl QUBRHRAWRVZUFZ-UHFFFAOYSA-N 0.000 claims 2
- 230000002194 synthesizing effect Effects 0.000 claims 2
- 238000002156 mixing Methods 0.000 claims 1
- 238000003756 stirring Methods 0.000 claims 1
- 238000001179 sorption measurement Methods 0.000 abstract description 42
- 230000015572 biosynthetic process Effects 0.000 abstract description 12
- 238000003786 synthesis reaction Methods 0.000 abstract description 12
- 238000000746 purification Methods 0.000 abstract description 4
- 230000007613 environmental effect Effects 0.000 abstract description 2
- 238000005292 vacuum distillation Methods 0.000 abstract description 2
- 238000000034 method Methods 0.000 description 16
- 230000000694 effects Effects 0.000 description 9
- 235000019647 acidic taste Nutrition 0.000 description 8
- 238000000926 separation method Methods 0.000 description 8
- 239000007788 liquid Substances 0.000 description 7
- 125000002883 imidazolyl group Chemical group 0.000 description 6
- 229920000642 polymer Polymers 0.000 description 6
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical group [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 5
- 238000010828 elution Methods 0.000 description 5
- 229920000831 ionic polymer Polymers 0.000 description 5
- 125000000524 functional group Chemical group 0.000 description 4
- 239000000463 material Substances 0.000 description 4
- 239000002904 solvent Substances 0.000 description 4
- JPVYNHNXODAKFH-UHFFFAOYSA-N Cu2+ Chemical compound [Cu+2] JPVYNHNXODAKFH-UHFFFAOYSA-N 0.000 description 3
- 238000005033 Fourier transform infrared spectroscopy Methods 0.000 description 3
- WAEMQWOKJMHJLA-UHFFFAOYSA-N Manganese(2+) Chemical compound [Mn+2] WAEMQWOKJMHJLA-UHFFFAOYSA-N 0.000 description 3
- PTFCDOFLOPIGGS-UHFFFAOYSA-N Zinc dication Chemical compound [Zn+2] PTFCDOFLOPIGGS-UHFFFAOYSA-N 0.000 description 3
- 238000010521 absorption reaction Methods 0.000 description 3
- 238000004821 distillation Methods 0.000 description 3
- 239000013067 intermediate product Substances 0.000 description 3
- 150000002500 ions Chemical class 0.000 description 3
- 150000002739 metals Chemical class 0.000 description 3
- 239000002245 particle Substances 0.000 description 3
- 239000000126 substance Substances 0.000 description 3
- WSLDOOZREJYCGB-UHFFFAOYSA-N 1,2-Dichloroethane Chemical group ClCCCl WSLDOOZREJYCGB-UHFFFAOYSA-N 0.000 description 2
- VTLYFUHAOXGGBS-UHFFFAOYSA-N Fe3+ Chemical compound [Fe+3] VTLYFUHAOXGGBS-UHFFFAOYSA-N 0.000 description 2
- ZOKXTWBITQBERF-UHFFFAOYSA-N Molybdenum Chemical compound [Mo] ZOKXTWBITQBERF-UHFFFAOYSA-N 0.000 description 2
- 238000005452 bending Methods 0.000 description 2
- 229910052799 carbon Inorganic materials 0.000 description 2
- 230000007423 decrease Effects 0.000 description 2
- 238000005265 energy consumption Methods 0.000 description 2
- 238000005342 ion exchange Methods 0.000 description 2
- 229910052750 molybdenum Inorganic materials 0.000 description 2
- 239000011733 molybdenum Substances 0.000 description 2
- 238000002414 normal-phase solid-phase extraction Methods 0.000 description 2
- 238000004064 recycling Methods 0.000 description 2
- 125000000391 vinyl group Chemical group [H]C([*])=C([H])[H] 0.000 description 2
- OVISMSJCKCDOPU-UHFFFAOYSA-N 1,6-dichlorohexane Chemical compound ClCCCCCCCl OVISMSJCKCDOPU-UHFFFAOYSA-N 0.000 description 1
- MLRVZFYXUZQSRU-UHFFFAOYSA-N 1-chlorohexane Chemical compound CCCCCCCl MLRVZFYXUZQSRU-UHFFFAOYSA-N 0.000 description 1
- CWYNVVGOOAEACU-UHFFFAOYSA-N Fe2+ Chemical compound [Fe+2] CWYNVVGOOAEACU-UHFFFAOYSA-N 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 125000000217 alkyl group Chemical group 0.000 description 1
- 238000004458 analytical method Methods 0.000 description 1
- 238000005349 anion exchange Methods 0.000 description 1
- 238000012512 characterization method Methods 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 238000003795 desorption Methods 0.000 description 1
- 238000000909 electrodialysis Methods 0.000 description 1
- 238000002474 experimental method Methods 0.000 description 1
- 238000000605 extraction Methods 0.000 description 1
- 239000000706 filtrate Substances 0.000 description 1
- 230000003993 interaction Effects 0.000 description 1
- 238000000622 liquid--liquid extraction Methods 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 238000002844 melting Methods 0.000 description 1
- 230000008018 melting Effects 0.000 description 1
- 239000012528 membrane Substances 0.000 description 1
- 229910021645 metal ion Inorganic materials 0.000 description 1
- 239000007769 metal material Substances 0.000 description 1
- 238000003921 particle size analysis Methods 0.000 description 1
- 239000003208 petroleum Substances 0.000 description 1
- 125000001997 phenyl group Chemical group [H]C1=C([H])C([H])=C(*)C([H])=C1[H] 0.000 description 1
- 238000006116 polymerization reaction Methods 0.000 description 1
- 230000008092 positive effect Effects 0.000 description 1
- 229910052700 potassium Inorganic materials 0.000 description 1
- 239000011591 potassium Substances 0.000 description 1
- 238000001556 precipitation Methods 0.000 description 1
- 239000000047 product Substances 0.000 description 1
- 230000008929 regeneration Effects 0.000 description 1
- 238000011069 regeneration method Methods 0.000 description 1
- 238000001878 scanning electron micrograph Methods 0.000 description 1
- 238000004626 scanning electron microscopy Methods 0.000 description 1
- 150000003334 secondary amides Chemical class 0.000 description 1
- 238000000638 solvent extraction Methods 0.000 description 1
- 239000002351 wastewater Substances 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
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- 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
- B01J20/26—Synthetic macromolecular compounds
- B01J20/264—Synthetic macromolecular compounds derived from different types of monomers, e.g. linear or branched copolymers, block copolymers, graft copolymers
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Abstract
本发明涉及一种聚咪唑类离子液体基共聚物及其制备方法和应用。属于吸附剂合成领域。取N‑乙烯咪唑与二氯烷烃加入到反应器中,再加入乙腈,混合均匀,于70‑80℃下反应8‑12h,减压蒸馏去除乙腈,洗涤,纯化,得到咪唑类离子液体[CxVmir][Cl];将咪唑类离子液体[CxVmir][Cl]、N,N‑亚甲基双丙烯酰胺MBA、二乙烯基苯DVB和乙腈超声搅拌均匀,加入过硫酸钾,于70‑80℃下反应18‑24h,冷却后,抽滤,洗涤,纯化,真空干燥,得到目标产物聚咪唑类离子液体基共聚物DVB‑p[CxVmir][Cl]。本发明制备方法简单、安全,对铼的吸附效率高,节能环保、吸附量大、具有实际应用性。
The invention relates to a polyimidazole ionic liquid-based copolymer and a preparation method and application thereof. It belongs to the field of adsorbent synthesis. Take N-vinylimidazole and dichloroalkane and add them to the reactor, then add acetonitrile, mix evenly, react at 70-80 ° C for 8-12 h, remove acetonitrile by vacuum distillation, wash and purify to obtain imidazole ionic liquid [C x Vmir][Cl]; the imidazole ionic liquid [C x Vmir][Cl], N,N-methylenebisacrylamide MBA, divinylbenzene DVB and acetonitrile were stirred uniformly by ultrasonic, and potassium persulfate was added to the React at 70-80°C for 18-24h, after cooling, suction filtration, washing, purification, and vacuum drying to obtain the target product polyimidazole ionic liquid-based copolymer DVB-p[C x Vmir][Cl]. The preparation method of the invention is simple and safe, has high adsorption efficiency for rhenium, energy saving and environmental protection, large adsorption capacity and practical applicability.
Description
技术领域technical field
本发明涉及聚离子液体基共聚物的制备方法及在环境及化工领域中的应用,具体涉及一种选择性吸附铼的聚咪唑类离子液体基共聚物吸附剂及其制备方法和应用。The invention relates to a preparation method of a polyionic liquid-based copolymer and its application in the environmental and chemical fields, in particular to a polyimidazole-based ionic liquid-based copolymer adsorbent for selectively adsorbing rhenium, and a preparation method and application thereof.
背景技术Background technique
稀散金属(缩写RSE)又可称为稀有分散金属,其中铼是一种贵重的稀散金属。它是地球上储量最稀少的金属,具有高强度、高熔点以及优异的延展性、机械稳定性、成形性,是当今重要的新兴金属材料,广泛应用于石油工业、航天工业、汽车工业、电子工业等现代工业各部门。Rare scattered metals (abbreviated RSE) can also be called rare scattered metals, of which rhenium is a precious rare metal. It is the rarest metal on earth with high strength, high melting point and excellent ductility, mechanical stability and formability. It is an important emerging metal material today and is widely used in petroleum industry, aerospace industry, automobile industry, electronics Industry and other modern industrial sectors.
目前提取铼的方法主要包括:萃取分离法、离子交换法、液膜法、氧化还原法、沉淀法和电渗析法等。这些方法最突出的缺点在于处理低浓度金属废水时操作繁琐,运行费用较高,耗能大,且易造成二次污染。吸附法分离的优点对环境不会产生污染,吸附能力强。At present, the methods of extracting rhenium mainly include: extraction separation method, ion exchange method, liquid membrane method, redox method, precipitation method and electrodialysis method. The most prominent shortcomings of these methods are that the operation is cumbersome, the operation cost is high, the energy consumption is high, and secondary pollution is easily caused when dealing with low-concentration metal wastewater. The advantages of adsorption separation are that it will not pollute the environment and has strong adsorption capacity.
离子液体作为一种新型的绿色溶剂,具有蒸气压低,离子电导率高,热稳定性以及化学稳定性好等优点。离子液体作为一种很好的吸附官能团,进行固化后不但能改善吸附材料的物理化学性质,而且能够克服在液液萃取中容易流失的问题,提高吸附材料的吸附能力与吸附选择性,因此在固相萃取方面也有很大的用途。聚合离子液体既具有离子液体的优点,又可以形成离子液体不具有的特殊形态与结构,同时在作为吸附材料方面又引入了有效官能团,因此近几年聚合离子液体在固相萃取方面有较多的研究。As a new type of green solvent, ionic liquids have the advantages of low vapor pressure, high ionic conductivity, good thermal stability and chemical stability. As a good adsorption functional group, ionic liquid can not only improve the physical and chemical properties of the adsorption material after curing, but also overcome the problem of easy loss in liquid-liquid extraction and improve the adsorption capacity and adsorption selectivity of the adsorption material. Solid phase extraction is also very useful. Polymeric ionic liquids not only have the advantages of ionic liquids, but also can form special shapes and structures that ionic liquids do not have. At the same time, they have introduced effective functional groups as adsorbent materials. Therefore, in recent years, polymeric ionic liquids have been widely used in solid phase extraction. Research.
发明内容SUMMARY OF THE INVENTION
本发明目的是提供一种聚咪唑类离子液体基共聚物,用聚离子液体作为吸附功能基团合成共聚物吸附剂。该吸附剂制备方法简单,再生能力强,对Re(VII)具有很高的吸附容量,可以从含铼溶液中很好的选择性吸附铼。本发明安全、节能环保、具有实际应用性。The object of the present invention is to provide a polyimidazole ionic liquid-based copolymer, which uses the polyionic liquid as an adsorption functional group to synthesize a copolymer adsorbent. The adsorbent has a simple preparation method, strong regeneration ability, high adsorption capacity for Re(VII), and can well selectively adsorb rhenium from a rhenium-containing solution. The invention is safe, energy-saving and environment-friendly, and has practical applicability.
本发明目的是通过如下技术方案实现的:一种聚咪唑类离子液体基共聚物,所述的聚咪唑类离子液体基共聚物为DVB-p[CxVmir][Cl],其中x=2、4、6;是以咪唑类离子液体为单体,N,N-亚甲基双丙烯酰胺MBA为交联剂,二乙烯基苯DVB作为基本骨架,通过自由基聚合反应合成。The object of the present invention is achieved through the following technical solutions: a polyimidazole-based ionic liquid-based copolymer, wherein the polyimidazole-based ionic liquid-based copolymer is DVB-p[C x Vmir][Cl], wherein x=2 , 4, 6; using imidazole ionic liquid as the monomer, N,N-methylenebisacrylamide MBA as the crosslinking agent, and divinylbenzene DVB as the basic skeleton, it is synthesized by free radical polymerization.
一种聚咪唑类离子液体基共聚物的制备方法,包括如下步骤:A preparation method of polyimidazole ionic liquid-based copolymer, comprising the following steps:
1)咪唑类离子液体的合成:取N-乙烯咪唑与二氯烷烃加入到反应器中,再加入乙腈,混合均匀,于70-80℃下反应8-12h,减压蒸馏去除乙腈,洗涤,纯化,得到咪唑类离子液体[CxVmir][Cl];1) Synthesis of imidazole ionic liquid: take N-vinylimidazole and dichloroalkane into the reactor, then add acetonitrile, mix well, react at 70-80 ° C for 8-12 h, remove acetonitrile by vacuum distillation, wash, Purification to obtain imidazole ionic liquid [C x Vmir][Cl];
2)聚咪唑类离子液体基共聚物的合成:将咪唑类离子液体[CxVmir][Cl]、N,N-亚甲基双丙烯酰胺MBA、二乙烯基苯DVB和乙腈超声搅拌均匀,加入过硫酸钾,于70-80℃下反应18-24h,冷却后,抽滤,洗涤,纯化,真空干燥,得到目标产物聚咪唑类离子液体基共聚物DVB-p[CxVmir][Cl],其中x=2、4、6。2) Synthesis of polyimidazole-based ionic liquid-based copolymer: The imidazole-based ionic liquid [C x Vmir][Cl], N,N-methylenebisacrylamide MBA, divinylbenzene DVB and acetonitrile were stirred uniformly by ultrasonic wave, Add potassium persulfate, react at 70-80 ℃ for 18-24h, after cooling, suction filter, wash, purify, and vacuum dry to obtain the target product polyimidazole ionic liquid-based copolymer DVB-p[C x Vmir][Cl ], where x=2, 4, 6.
优选的,上述的一种聚咪唑类离子液体基共聚物的制备方法,按摩尔比,N-乙烯咪唑:二氯烷烃为0.33-4.00:1。Preferably, in the above-mentioned preparation method of a polyimidazole ionic liquid-based copolymer, the molar ratio of N-vinylimidazole:dichloroalkane is 0.33-4.00:1.
优选的,上述的一种聚咪唑类离子液体基共聚物的制备方法,所述的二氯烷烃为1,2-二氯乙烷、1,4-二氯丁烷、或1,6-二氯己烷。Preferably, in the above-mentioned preparation method of a polyimidazole ionic liquid-based copolymer, the dichloroalkane is 1,2-dichloroethane, 1,4-dichlorobutane, or 1,6-dichlorobutane Chlorohexane.
优选的,上述的一种聚咪唑类离子液体基共聚物的制备方法,咪唑类离子液体[CxVmir][Cl]、N,N-亚甲基双丙烯酰胺MBA、二乙烯基苯DVB和过硫酸钾之间的质量比为1:2.42×10-3-7.25×10-3:0.07-0.86:0.04-0.05。Preferably, the above-mentioned preparation method of a polyimidazole ionic liquid-based copolymer comprises imidazole ionic liquids [C x Vmir][Cl], N,N-methylenebisacrylamide MBA, divinylbenzene DVB and The mass ratio between potassium persulfates is 1:2.42×10 −3 −7.25×10 −3 :0.07-0.86:0.04-0.05.
上述的聚咪唑类离子液体基共聚物作为吸附剂在回收稀散金属铼中的应用。方法如下:于含有铼的溶液中,调节溶液的pH为1-7,加入上述的聚咪唑类离子液体基共聚物DVB-p[CxVmir][Cl],振荡吸附8-10h后,用洗脱剂进行洗脱。The application of the above-mentioned polyimidazole ionic liquid-based copolymer as an adsorbent in recovering scattered metal rhenium. The method is as follows: in a solution containing rhenium, adjust the pH of the solution to 1-7, add the above-mentioned polyimidazole ionic liquid-based copolymer DVB-p[C x Vmir][Cl], and after oscillating and adsorbing for 8-10 hours, use eluent to elute.
优选的,调节溶液的pH为3。Preferably, the pH of the adjusted solution is 3.
优选的,所述的洗脱剂为盐酸。更优选的,所述的洗脱剂为体积百分浓度为1~10%的盐酸。Preferably, the eluent is hydrochloric acid. More preferably, the eluent is hydrochloric acid with a volume percent concentration of 1-10%.
与现有技术相比,本发明具有以下优点和积极效果:Compared with the prior art, the present invention has the following advantages and positive effects:
(1)本发明制备出的聚咪唑类离子液体基共聚物作为吸附剂分离效率高,可从混合离子溶液中高选择性的吸附铼,具有吸附量大和多次循环利用性能,适用范围广,具有实际应用性。(1) The polyimidazole ionic liquid-based copolymer prepared by the present invention has high separation efficiency as an adsorbent, can adsorb rhenium with high selectivity from mixed ionic solutions, has large adsorption capacity and multiple recycling performance, has a wide range of applications, and has practical applicability.
(2)本发明合成过程条件容易控制,能耗低,操作简单,属于清洁生产工艺,易于工业化生产。(2) The synthesis process conditions of the present invention are easy to control, the energy consumption is low, and the operation is simple, which belongs to the clean production process and is easy to be industrialized.
(3)本发明吸附速度快,解吸性能好,选择性高,对Re(VII)的最大吸附量可达517.61mg·g-1。(3) The invention has fast adsorption speed, good desorption performance and high selectivity, and the maximum adsorption amount of Re(VII) can reach 517.61 mg·g -1 .
(4)本发明以聚离子液体为功能基团,以MBA为交联剂,DVB为基本骨架通过自由基聚合反应间接合成聚合物吸附剂,用于对水中Re(VII)的吸附。该吸附剂的制备方法简单,安全,成本低,分离富集效率高,可从Cu(II)、Fe(II)、Zn(II)、Mn(II)、Mo(VI)等共存离子溶液中选择性的吸附Re(VII)。(4) In the present invention, polyionic liquid is used as functional group, MBA is used as crosslinking agent, and DVB is used as basic skeleton to indirectly synthesize polymer adsorbent through radical polymerization reaction, which is used for the adsorption of Re(VII) in water. The preparation method of the adsorbent is simple, safe, low in cost and high in separation and enrichment efficiency, and can be obtained from coexisting ionic solutions such as Cu(II), Fe(II), Zn(II), Mn(II), Mo(VI), etc. Selective adsorption of Re(VII).
附图说明Description of drawings
图1a为实施例1制备的DVB-p[C2Vmir][Cl]的FT-IR图。FIG. 1a is the FT-IR image of DVB-p[C 2 Vmir][Cl] prepared in Example 1. FIG.
图1b为实施例1制备的DVB-p[C4Vmir][Cl]的FT-IR图。FIG. 1b is the FT-IR image of DVB-p[C 4 Vmir][Cl] prepared in Example 1. FIG.
图1c为实施例1制备的DVB-p[C6Vmir][Cl]的FT-IR图。FIG. 1 c is the FT-IR image of DVB-p[C 6 Vmir][Cl] prepared in Example 1. FIG.
图2为聚咪唑类离子液体基共聚物的SEM图;Fig. 2 is the SEM image of polyimidazole ionic liquid-based copolymer;
其中,a:DVB-p[C2Vmir][Cl];b:DVB-p[C4Vmir][Cl];c:DVB-p[C6Vmir][Cl]。Wherein, a: DVB-p[C 2 Vmir][Cl]; b: DVB-p[C 4 Vmir][Cl]; c: DVB-p[C 6 Vmir][Cl].
图3是DVB-p[C2Vmir][Cl],DVB-p[C4Vmir][Cl],DVB-p[C6Vmir][Cl]在不同酸度下对吸附Re(VII)的影响。Figure 3 shows the effects of DVB-p[C 2 Vmir][Cl], DVB-p[C 4 Vmir][Cl], DVB-p[C 6 Vmir][Cl] on the adsorption of Re(VII) at different acidities .
图4是DVB-p[C4Vmir][Cl]吸附Re(VII)的吸附等温线。Figure 4 is an adsorption isotherm of DVB-p[C 4 Vmir][Cl] adsorbing Re(VII).
图5是DVB-p[C4Vmir][Cl]在不同酸度下对Re(VII)的选择性。Figure 5 is the selectivity of DVB-p[C 4 Vmir][Cl] for Re(VII) at different acidities.
图6是DVB-p[C6Vmir][Cl]在不同酸度下对Re(VII)的选择性。Figure 6 is the selectivity of DVB-p[C6Vmir][Cl] for Re(VII) at different acidity.
具体实施方式Detailed ways
为了更好地理解本发明的技术方案,特以具体的实施例作进一步详细说明,但方案不限于此。In order to better understand the technical solutions of the present invention, specific embodiments are used for further detailed description, but the solutions are not limited thereto.
实施例1一种聚咪唑类离子液体基共聚物Embodiment 1 A kind of polyimidazole ionic liquid-based copolymer
(一)聚咪唑类离子液体基共聚物DVB-p[C2Vmir][Cl](1) Polyimidazole ionic liquid-based copolymer DVB-p[C 2 Vmir][Cl]
制备方法如下:The preparation method is as follows:
1)咪唑类离子液体的合成:取4.706g N-乙烯咪唑与9.896g1,2-二氯乙烷加入到100mL单口烧瓶中,再加入40mL乙腈混合均匀,80℃下反应9h,得到棕色粘稠状的液体,用减压蒸馏去除乙腈,洗涤,纯化得到中间产物咪唑类离子液体[C2Vmir][Cl]。1) Synthesis of imidazole ionic liquid: take 4.706g of N-vinylimidazole and 9.896g of 1,2-dichloroethane into a 100mL single-neck flask, then add 40mL of acetonitrile to mix evenly, and react at 80°C for 9h to obtain a brown viscous The acetonitrile was removed by distillation under reduced pressure, washed and purified to obtain the intermediate product imidazole ionic liquid [C 2 Vmir][Cl].
2)将4mL所得[C2Vmir][Cl]加入三口烧瓶中,之后再加入0.02g N,N-亚甲基双丙烯酰胺(MBA),0.3mL二乙烯基苯(DVB),40mL乙腈,超声20min,再加入0.2g过硫酸钾,80℃下反应24h,冷却后,抽滤,洗涤,纯化,真空干燥,得到聚咪唑类离子液体基共聚物DVB-p[C2Vmir][Cl]。2) Add 4 mL of the obtained [C 2 Vmir][Cl] into the three-necked flask, and then add 0.02 g of N,N-methylenebisacrylamide (MBA), 0.3 mL of divinylbenzene (DVB), and 40 mL of acetonitrile, Ultrasonic for 20min, then add 0.2g potassium persulfate, react at 80℃ for 24h, after cooling, suction filter, wash, purify, and vacuum dry to obtain polyimidazole ionic liquid-based copolymer DVB-p[C 2 Vmir][Cl] .
(二)聚咪唑类离子液体基共聚物DVB-p[C4Vmir][Cl](2) Polyimidazole ionic liquid-based copolymer DVB-p[C 4 Vmir][Cl]
制备方法如下:The preparation method is as follows:
1)咪唑类离子液体的合成,取4.706g N-乙烯咪唑与12.701g1,4-二氯丁烷加入到100mL单口烧瓶中,再加入40mL乙腈混合均匀,80℃下反应9h,得到棕色粘稠状的液体,用减压蒸馏去除乙腈,洗涤纯化得到中间产物咪唑类离子液体[C4Vmir][Cl]。1) Synthesis of imidazole ionic liquid, take 4.706g of N-vinylimidazole and 12.701g of 1,4-dichlorobutane into a 100mL single-neck flask, then add 40mL of acetonitrile to mix evenly, and react at 80°C for 9h to obtain a brown viscous The acetonitrile was removed by distillation under reduced pressure, washed and purified to obtain the intermediate product imidazole ionic liquid [C 4 Vmir][Cl].
2)将4mL所得[C4Vmir][Cl]加入三口烧瓶中,之后再加入0.02g N,N-亚甲基双丙烯酰胺(MBA),0.3mL二乙烯基苯(DVB),40mL乙腈,超声20min,再加入0.2g过硫酸钾80℃下反应24h,冷却后,抽滤,洗涤,纯化,真空干燥,得到聚咪唑类离子液体基共聚物DVB-p[C4Vmir][Cl]。2) Add 4 mL of the obtained [C 4 Vmir][Cl] into the three-necked flask, and then add 0.02 g of N,N-methylenebisacrylamide (MBA), 0.3 mL of divinylbenzene (DVB), and 40 mL of acetonitrile, Sonicate for 20 min, then add 0.2 g of potassium persulfate and react at 80°C for 24 h. After cooling, suction filtration, washing, purification, and vacuum drying to obtain polyimidazole ionic liquid-based copolymer DVB-p[C 4 Vmir][Cl].
(三)聚咪唑类离子液体基共聚物DVB-p[C6Vmir][Cl](3) Polyimidazole ionic liquid-based copolymer DVB-p[C 6 Vmir][Cl]
制备方法如下:The preparation method is as follows:
1)咪唑类离子液体的合成,取4.706g N-乙烯咪唑与15.506g1,6-二氯己烷加入到250mL单口烧瓶中,再加入40mL乙腈混合均匀,80℃下反应9h,得到棕色粘稠状的液体,用减压蒸馏去除溶剂,洗涤纯化得到中间产物咪唑类离子液体[C6Vmir][Cl]。1) Synthesis of imidazole ionic liquid, take 4.706g of N-vinylimidazole and 15.506g of 1,6-dichlorohexane into a 250mL single-neck flask, then add 40mL of acetonitrile to mix evenly, and react at 80°C for 9h to obtain a brown viscous The solvent was removed by distillation under reduced pressure, washed and purified to obtain the intermediate product imidazole ionic liquid [C 6 Vmir][Cl].
2)将4mL所得[C6Vmir][Cl]加入三口烧瓶中,之后再加入0.02g N,N-亚甲基双丙烯酰胺(MBA),0.3mL二乙烯基苯(DVB),40mL乙腈,超声20min,再加入0.2g过硫酸钾80℃下反应24h,冷却后,抽滤,洗涤,纯化,真空干燥,得到聚咪唑类离子液体基共聚物DVB-p[C6Vmir][Cl]。2) Add 4 mL of the obtained [C 6 Vmir][Cl] into the three-necked flask, then add 0.02 g of N,N-methylenebisacrylamide (MBA), 0.3 mL of divinylbenzene (DVB), 40 mL of acetonitrile, Sonicate for 20 min, then add 0.2 g of potassium persulfate and react at 80°C for 24 h. After cooling, suction filtration, washing, purification, and vacuum drying to obtain polyimidazole ionic liquid-based copolymer DVB-p[C 6 Vmir][Cl].
(四)表征:(4) Characterization:
1)IR分析:结果如图1a、图1b和图1c所示,由图1b可以看出[C4Vmir][Cl]在1638cm-1是N-乙烯基咪唑上乙烯基的C=C以及咪唑环中的C=C和C=N的伸缩振动峰,在3108和3065cm-1处都出现C=C中C-H的伸缩振动峰以及咪唑环上的C-H的伸缩振动峰,这可以证明[C4Vmir][Cl]的成功合成。由图1a和图1c同理证明[C2Vmir][Cl]和[C6Vmir][Cl]成功合成。1) IR analysis: the results are shown in Figure 1a, Figure 1b and Figure 1c, it can be seen from Figure 1b that [C 4 Vmir][Cl] at 1638 cm -1 is the C=C of the vinyl group on N-vinylimidazole and The stretching vibration peaks of C=C and C=N in the imidazole ring, the stretching vibration peaks of CH in C=C and the stretching vibration peaks of CH on the imidazole ring appear at 3108 and 3065 cm -1 , which can prove that [C 4 Successful synthesis of Vmir][Cl]. [C 2 Vmir][Cl] and [C 6 Vmir][Cl] were successfully synthesized from Fig. 1a and Fig. 1c.
对比图1b中DVB-p[C4Vmir][Cl]和[C4Vmir][Cl]的红外图,可以看出DVB-p[C4Vmir][Cl]中1638cm-1处吸收峰变弱,是由于N-乙烯咪唑上乙烯基的C=C的伸缩振动峰参与了反应,N-乙烯咪唑中的C=N的伸缩振动峰依然存在;而3108cm-1处的C=C中的C-H的伸缩振动峰消失;还可以发现在3500cm-1处存在明显的N-H的伸缩振动峰,这说明合成过程发生了自由基聚合反应。另外在DVB-p[C4Vmir][Cl]中1655cm-1处还出现仲酰胺的C=O的伸缩振动峰,这说明MBA也参与了聚合反应;除此之外在1640cm-1左右处的弯曲振动峰变宽,说明苯环的吸收峰与咪唑环的特征吸收峰重叠,这可以说明DVB参与了自由基聚合反应。综上所述,说明DVB-p[C4Vmir][Cl]的成功合成。由图1a和图1c同理证明DVB-p[C2Vmir][Cl]和DVB-p[C6Vmir][Cl]的成功合成。Comparing the infrared images of DVB-p[C 4 Vmir][Cl] and [C 4 Vmir][Cl] in Fig. 1b, it can be seen that the absorption peak at 1638 cm -1 in DVB-p[C 4 Vmir][Cl] changes. Weak, because the stretching vibration peak of C=C of vinyl group on N-vinylimidazole participates in the reaction, the stretching vibration peak of C=N in N - vinylimidazole still exists; The stretching vibration peak of CH disappears; it can also be found that there is an obvious stretching vibration peak of NH at 3500 cm -1 , which indicates that free radical polymerization occurs in the synthesis process. In addition, in DVB-p[C 4 Vmir][Cl], the stretching vibration peak of C=O of secondary amide also appeared at 1655cm -1 , which indicated that MBA also participated in the polymerization; The flexural vibration peaks of , show that the absorption peak of the benzene ring overlaps with the characteristic absorption peak of the imidazole ring, which can indicate that DVB participates in the radical polymerization reaction. In conclusion, the successful synthesis of DVB-p[C 4 Vmir][Cl] is demonstrated. The successful synthesis of DVB-p[C 2 Vmir][Cl] and DVB-p[C 6 Vmir][Cl] is similarly proved from Figure 1a and Figure 1c.
2)SEM和粒径分析:三种聚合物DVB-p[C2Vmir][Cl],DVB-p[C4Vmir][Cl]和DVB-p[C6Vmir][Cl]的平均粒径随着离子液体烷基链的增加而增加,分别是6.21,8.24,8.38μm。SEM结果如图2所示,从图2中可以明显看到三种聚合物的微观形貌是不同的,图2中(a)是DVB-p[C2Vmir][Cl]的微观形貌图,可以明显看到聚集状的海绵片状结构;图2中(b)中DVB-p[C4Vmir][Cl]的微观形貌是清晰的相对较分散的片状结构,片状之间的分界较为明显;图2中(c)是DVB-p[C6Vmir][Cl]的微观结构呈现出许多球形结构。这是因为不同碳链长度的聚离子液体在合成过程中发生了变化,碳链较长的聚离子液体基共聚物会发生弯曲变化,使其呈现球状结构,从而也导致聚合物的粒径变大;另外,共聚物与溶剂间的“热力学效应”也会促使其分子链弯曲使其聚集体形成球状结构,这种现象可以减少聚集体与溶剂的接触。所以其粒径随着碳链长度的增加而增加,微观呈现球状结构。2) SEM and particle size analysis: average particle size of three polymers DVB-p[C 2 Vmir][Cl], DVB-p[C 4 Vmir][Cl] and DVB-p[C 6 Vmir][Cl] The diameters increased with the increase of the alkyl chain of the ionic liquid, which were 6.21, 8.24, and 8.38 μm, respectively. The SEM results are shown in Figure 2. It can be clearly seen from Figure 2 that the microscopic morphologies of the three polymers are different. Figure 2 (a) is the microscopic morphology of DVB-p[C 2 Vmir][Cl]. In Figure 2, the aggregated sponge sheet structure can be clearly seen; the microscopic morphology of DVB-p[C 4 Vmir][Cl] in Figure 2 (b) is a clear and relatively dispersed sheet structure. The boundary between them is more obvious; Fig. 2(c) is the microstructure of DVB-p[C 6 Vmir][Cl] showing many spherical structures. This is because polyionic liquids with different carbon chain lengths have changed during the synthesis process, and polyionic liquid-based copolymers with longer carbon chains will undergo bending changes, making them spherical structures, which also lead to changes in the particle size of the polymer. In addition, the "thermodynamic effect" between the copolymer and the solvent will also promote the bending of its molecular chain to make the aggregate form a spherical structure, which can reduce the contact between the aggregate and the solvent. Therefore, the particle size increases with the increase of the carbon chain length, and the microscopically presents a spherical structure.
实施例2聚咪唑类离子液体基共聚物作为吸附剂对铼的回收Example 2 Recovery of rhenium by polyimidazole ionic liquid-based copolymer as adsorbent
(一)不同碳链长度聚咪唑类离子液体基共聚物吸附剂对Re(VII)的吸附影响(1) Adsorption effect of polyimidazole ionic liquid-based copolymer adsorbents with different carbon chain lengths on Re(VII)
方法:分别取10mg实施例1制备的聚合物DVB-p[C2Vmir][Cl]、DVB-p[C4Vmir][Cl]、DVB-p[C6Vmir][Cl],分别加入不同pH(pH=1,2,3,4,5,6,7)5mL,20mg·L-1Re(VII)的溶液,将其在振荡箱中振荡8h,结果如图3所示。Method: Take 10 mg of polymers DVB-p[C 2 Vmir][Cl], DVB-p[C 4 Vmir][Cl], DVB-p[C 6 Vmir][Cl] prepared in Example 1, respectively, add Different pH (pH=1, 2, 3, 4, 5, 6, 7) 5 mL, 20 mg·L -1 Re(VII) solutions were shaken in a shaking box for 8 h, and the results are shown in Figure 3 .
由图3可知,可以看出在高酸条件下三种吸附剂对Re(VII)的吸附能力都比较低,这可能是因为在较高酸度下溶液中的Cl-浓度较高,不利于吸附材料上的Cl-与ReO4 -发生阴离子交换;在较低酸度下,ReO4 -与咪唑环静电引力作用增强,从而使吸附能力提高,DVB-p[C4Vmir][Cl]与DVB-p[C6Vmir][Cl]吸附量的变化趋势相似,随着pH的增加,吸附量迅速升高,在pH 3处达到最大吸附量分别为97.00%和98.20%,随后吸附量稍有降低,在pH 6处达到最低分别为91.06%和92.70%,而DVB-p[C2Vmir][Cl]的吸附量也在pH 3时达到最高为92.58%,但随着pH继续增加,吸附量下降较为明显,在pH 6时已降至73.65%;DVB-p[C4Vmir][Cl]和DVB-p[C6Vmir][Cl]在不同酸度条件下对Re(VII)的吸附能力都高于DVB-p[C2Vmir][Cl],这可能是因为DVB-p[C2Vmir][Cl]碳链短,其中Cl-与咪唑环的静电作用力较大,不利于与溶液中ReO4 -发生离子交换作用,所以不利于Re(VII)的吸附。As can be seen from Figure 3, it can be seen that the adsorption capacity of the three adsorbents for Re(VII) is relatively low under high acid conditions, which may be because the Cl - concentration in the solution is higher at higher acidity, which is not conducive to adsorption. The Cl - on the material undergoes anion exchange with ReO 4 - ; at lower acidity, the electrostatic attraction between ReO 4 - and the imidazole ring is enhanced, thereby improving the adsorption capacity, DVB-p[C 4 Vmir][Cl] and DVB- The variation trend of the adsorption capacity of p[C 6 Vmir][Cl] is similar, with the increase of pH, the adsorption capacity increases rapidly, reaching the maximum adsorption capacity of 97.00% and 98.20% at pH 3, and then the adsorption capacity decreases slightly , reaching a minimum of 91.06% and 92.70% at pH 6, respectively, while the adsorption capacity of DVB-p[ C2Vmir ][Cl] also reached a maximum of 92.58% at pH 3, but as the pH continued to increase, the adsorption capacity The decrease is more obvious, and it has dropped to 73.65% at pH 6; the adsorption capacity of DVB-p[C 4 Vmir][Cl] and DVB-p[C 6 Vmir][Cl] for Re(VII) under different acidity conditions are higher than DVB-p[C 2 Vmir][Cl], which may be due to the short carbon chain of DVB-p[C 2 Vmir][Cl], in which the electrostatic force between Cl - and imidazole ring is large, which is not conducive to the interaction with the imidazole ring. ReO 4 - in the solution undergoes ion exchange, so it is not conducive to the adsorption of Re(VII).
(二)不同Re(VII)的浓度对吸附的影响(2) The effect of different Re(VII) concentrations on adsorption
方法:取10mg实施例1制备的聚合物DVB-p[C4Vmir][Cl],分别加入5mLpH=3,Re(VII)浓度分别为20mg·L-1、50mg·L-1、100mg·L-1、200mg·L-1、300mg·L-1、400mg·L-1、500mg·L-1、800mg·L-1的含铼溶液中,将其在振荡箱中振荡8h,结果如图4所示。Method: Take 10 mg of the polymer DVB-p[C 4 Vmir][Cl] prepared in Example 1, add 5 mL of pH=3 respectively, and the concentrations of Re(VII) are 20 mg·L -1 , 50 mg·L -1 , 100 mg· L -1 , 200mg·L -1 , 300mg·L -1 , 400mg·L -1 , 500mg·L -1 , 800mg·L -1 containing rhenium solution, shake it in a shaking box for 8h, the results are as follows shown in Figure 4.
由图4可见,低浓度时,吸附量随着Re(VII)的浓度的增大而增大,DVB-p[C4Vmir][Cl]对铼的吸附量qe达到517.61mg·g-1时趋于平衡。从不同类型吸附等温线拟合的相关系数可以得出吸附符合Langmuir吸附等温模型。It can be seen from Fig. 4 that at low concentration, the adsorption amount increases with the increase of Re(VII) concentration, and the adsorption amount q e of DVB-p[C 4 Vmir][Cl] for rhenium reaches 517.61 mg·g − 1 o'clock tends to balance. From the correlation coefficients fitted by different types of adsorption isotherms, it can be concluded that the adsorption conforms to the Langmuir adsorption isotherm model.
(三)不同酸度下DVB-p[C4Vmir][Cl]吸附剂对混合金属溶液中Re(VII)的分离效果(3) Separation effect of DVB-p[C 4 Vmir][Cl] adsorbent on Re(VII) in mixed metal solution under different acidity
分别取含有Re(VII)、Cu(II)、Zn(II)、Mn(II)、Fe(III)、Mo(VI)20mg·L-1的溶液各10mL,分别调节溶液pH=1、2、3、4和5,然后加入10mg实施例1制备的DVB-p[C4Vmir][Cl]吸附剂,震荡8h,测定溶液中各离子浓度,结果如图5所示。Take 10 mL of each solution containing 20 mg·L -1 of Re(VII), Cu(II), Zn(II), Mn(II), Fe(III), and Mo(VI), respectively, and adjust the pH of the solution to 1, 2 , 3, 4 and 5, then add 10 mg of the DVB-p[C 4 Vmir][Cl] adsorbent prepared in Example 1, shake for 8 hours, and measure the concentration of each ion in the solution. The results are shown in Figure 5 .
由图5可以看出,在pH为3的时候,DVB-p[C4Vmir][Cl]对Re(VII)的吸附可以达到90%以上,而对除Mo(VI)之外的其他金属离子几乎不吸附,说明DVB-p[C4Vmir][Cl]对Re(VII)具有较高的选择性,而其它共存金属离子的干扰很小。It can be seen from Figure 5 that at pH 3, the adsorption of DVB-p[C 4 Vmir][Cl] for Re(VII) can reach more than 90%, while for other metals except Mo(VI) The ions were hardly adsorbed, indicating that DVB-p[C 4 Vmir][Cl] has high selectivity for Re(VII), while the interference of other coexisting metal ions is small.
(四)不同酸度下DVB-p[C6Vmir][Cl]吸附剂对混合金属溶液中Re(VII)的分离效果(4) Separation effect of DVB-p[C 6 Vmir][Cl] adsorbent on Re(VII) in mixed metal solution under different acidity
分别取含有Re(VII)、Cu(II)、Zn(II)、Mn(II)、Fe(III)、Mo(VI)20mg·L-1的溶液各10mL,分别调节溶液pH=1、2、3、4和5,然后加入10mg实施例1制备的DVB-p[C6Vmir][Cl]吸附剂,震荡8h,测定溶液中各离子浓度,结果如图6所示。Take 10 mL of each solution containing 20 mg·L -1 of Re(VII), Cu(II), Zn(II), Mn(II), Fe(III), and Mo(VI), respectively, and adjust the pH of the solution to 1, 2 , 3, 4 and 5, then add 10 mg of the DVB-p[C 6 Vmir][Cl] adsorbent prepared in Example 1, shake for 8 hours, and measure the concentration of each ion in the solution, the results are shown in Figure 6 .
由图6可以看出,在pH=1的时候,DVB-p[C6Vmir][Cl]对铼的吸附率可达到90%以上,而对钼几乎不吸附,说明DVB-p[C6Vmir][Cl]对Re(VII)具有更好的分离选择性,可实现混合料液中钼铼的分离。It can be seen from Fig. 6 that at pH=1, the adsorption rate of DVB-p[C 6 Vmir][Cl] to rhenium can reach more than 90%, while the adsorption of molybdenum is almost not, indicating that DVB-p[C 6 Vmir][Cl] has better separation selectivity for Re(VII), which can realize the separation of molybdenum and rhenium in the mixed feed liquid.
(五)不同洗脱剂对Re(VII)洗脱效果(5) Elution effect of different eluents on Re(VII)
方法:将100mg实施例1制备的DVB-p[C4Vmir][Cl]吸附剂置于100mLpH=3浓度为400mg·L-1的Re(VII)溶液中,室温下震荡8h达吸附饱和后过滤,干燥。称取干燥后吸附剂10mg,将其放入含有不同洗脱剂的小瓶中,在室温下震荡8h过滤,测定滤液中铼的浓度,结果如表1。Method: 100 mg of DVB-p[C 4 Vmir][Cl] adsorbent prepared in Example 1 was placed in 100 mL of Re(VII) solution with pH=3 concentration of 400 mg·L -1 , and shaken for 8 h at room temperature to reach adsorption saturation. Filter and dry. Weigh 10 mg of the dried adsorbent, put it into a vial containing different eluents, shake at room temperature for 8 h and filter, and measure the concentration of rhenium in the filtrate. The results are shown in Table 1.
表1实施例1制备的DVB-p[C4Vmir][Cl]吸附剂在不同洗脱剂下的洗脱率Table 1 Elution rate of DVB-p[C 4 Vmir][Cl] adsorbent prepared in Example 1 under different eluents
表1中表明,盐酸作为洗脱剂,效果显著,体积百分浓度为10%的盐酸对Re(VII)的解析效果最好,洗脱率可达96.79%。As shown in Table 1, hydrochloric acid as an eluent has a remarkable effect, and the hydrochloric acid with a concentration of 10% by volume has the best analytical effect on Re(VII), and the elution rate can reach 96.79%.
(六)吸附剂循环使用性能(6) Recycling performance of adsorbent
方法:称取100mg吸附剂置于100mL,pH=3,浓度为50mg·L-1的Re(VII)溶液中,室温下震荡8h吸附饱和后过滤,然后用4%的盐酸溶液进行洗脱,经过4次吸附-洗脱循环,结果如表2。Method: Weigh 100 mg of adsorbent and place it in 100 mL of Re(VII) solution with pH=3 and concentration of 50 mg·L -1 , shake at room temperature for 8 h after adsorption saturation, filter, and then elute with 4% hydrochloric acid solution, After 4 adsorption-elution cycles, the results are shown in Table 2.
表2实施例1制备的DVB-p[C4Vmir][Cl]吸附剂的循环实验Table 2 Cycle experiment of DVB-p[C 4 Vmir][Cl] adsorbent prepared in Example 1
由表2可见,经过4次吸附-洗脱循环后,吸附剂DVB-p[C4Vmir][Cl]对Re(VII)的吸附量仍能达到48.80mg·g-1,回收率可达95.59%,证明吸附剂DVB-p[C4Vmir][Cl]具有良好的稳定性和可再生性。It can be seen from Table 2 that after 4 adsorption-elution cycles, the adsorption capacity of the adsorbent DVB-p[C 4 Vmir][Cl] to Re(VII) can still reach 48.80 mg·g -1 , and the recovery rate can reach 48.80 mg·g -1 . 95.59%, which proves that the adsorbent DVB-p[C 4 Vmir][Cl] has good stability and reproducibility.
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Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN102050919A (en) * | 2010-11-12 | 2011-05-11 | 西北师范大学 | Supported imidazole ion liquid cross-linked polymer nano particles and preparation and application thereof |
CN104689807A (en) * | 2013-12-04 | 2015-06-10 | 中国科学院大连化学物理研究所 | Am imidazole dicationic ionic liquid hydrophilic interaction chromatography stationary phase, and preparation and applications thereof |
CN106824113A (en) * | 2017-03-07 | 2017-06-13 | 辽宁大学 | A kind of preparation and its application of glyoxaline ion liquid modification of chitosan adsorbent |
CN107486240A (en) * | 2017-05-19 | 2017-12-19 | 中国科学院兰州化学物理研究所 | A kind of ionic liquid cross-linked polymer load Technique of Nano Pd metal catalytic material and preparation method and application |
-
2018
- 2018-08-01 CN CN201810860452.5A patent/CN108912269B/en active Active
Patent Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN102050919A (en) * | 2010-11-12 | 2011-05-11 | 西北师范大学 | Supported imidazole ion liquid cross-linked polymer nano particles and preparation and application thereof |
CN104689807A (en) * | 2013-12-04 | 2015-06-10 | 中国科学院大连化学物理研究所 | Am imidazole dicationic ionic liquid hydrophilic interaction chromatography stationary phase, and preparation and applications thereof |
CN106824113A (en) * | 2017-03-07 | 2017-06-13 | 辽宁大学 | A kind of preparation and its application of glyoxaline ion liquid modification of chitosan adsorbent |
CN107486240A (en) * | 2017-05-19 | 2017-12-19 | 中国科学院兰州化学物理研究所 | A kind of ionic liquid cross-linked polymer load Technique of Nano Pd metal catalytic material and preparation method and application |
Non-Patent Citations (3)
Title |
---|
Preparation of ionic liquid hybrid melamine-based covalent organic polymer functionalized polymer monolithic material for the preconcentration of synthetic phenolic antioxidants;antioxidantsHuiqi Wang等;《Journal of Chromatography A》;20180621;第1566卷;23-31 * |
Selective adsorption of Re(VII) by chitosan modified with imidazolium-base ionic liquidd;Zhenning Lou等;《Hydrometallurgy》;20180529;第179卷;141-148 * |
Viologen-functionalized poly(ionic liquids): Spectroelectrochemical and QCM-D studies;Cíntia Marques Corrêa等;《Journal of Electroanalytical Chemistry》;20171108;第819卷;365-373 * |
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