CN115715976A - Selective Lithium Ion Adsorption Method Based on Protein/Inorganic Nanoparticle Composite Membrane - Google Patents
Selective Lithium Ion Adsorption Method Based on Protein/Inorganic Nanoparticle Composite Membrane Download PDFInfo
- Publication number
- CN115715976A CN115715976A CN202211509531.4A CN202211509531A CN115715976A CN 115715976 A CN115715976 A CN 115715976A CN 202211509531 A CN202211509531 A CN 202211509531A CN 115715976 A CN115715976 A CN 115715976A
- Authority
- CN
- China
- Prior art keywords
- protein
- inorganic nanoparticle
- nanoparticle composite
- lithium ions
- composite membrane
- 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.)
- Pending
Links
- 239000002131 composite material Substances 0.000 title claims abstract description 69
- 229910001416 lithium ion Inorganic materials 0.000 title claims abstract description 68
- HBBGRARXTFLTSG-UHFFFAOYSA-N Lithium ion Chemical compound [Li+] HBBGRARXTFLTSG-UHFFFAOYSA-N 0.000 title claims abstract description 66
- 239000012528 membrane Substances 0.000 title claims abstract description 58
- 238000001179 sorption measurement Methods 0.000 title claims abstract description 55
- 108090000623 proteins and genes Proteins 0.000 title claims abstract description 50
- 102000004169 proteins and genes Human genes 0.000 title claims abstract description 50
- 239000002105 nanoparticle Substances 0.000 title claims abstract description 46
- 238000000034 method Methods 0.000 title claims abstract description 18
- 235000018102 proteins Nutrition 0.000 claims abstract description 49
- GWEVSGVZZGPLCZ-UHFFFAOYSA-N Titan oxide Chemical compound O=[Ti]=O GWEVSGVZZGPLCZ-UHFFFAOYSA-N 0.000 claims abstract description 32
- 239000007864 aqueous solution Substances 0.000 claims abstract description 20
- 239000007788 liquid Substances 0.000 claims abstract description 13
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 13
- 108010073771 Soybean Proteins Proteins 0.000 claims abstract description 9
- 235000019710 soybean protein Nutrition 0.000 claims abstract description 9
- 239000004408 titanium dioxide Substances 0.000 claims abstract description 9
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 claims abstract description 8
- NUJOXMJBOLGQSY-UHFFFAOYSA-N manganese dioxide Chemical compound O=[Mn]=O NUJOXMJBOLGQSY-UHFFFAOYSA-N 0.000 claims abstract description 8
- 238000002360 preparation method Methods 0.000 claims abstract description 8
- 239000000463 material Substances 0.000 claims abstract description 7
- MCMNRKCIXSYSNV-UHFFFAOYSA-N ZrO2 Inorganic materials O=[Zr]=O MCMNRKCIXSYSNV-UHFFFAOYSA-N 0.000 claims abstract description 4
- DLINORNFHVEIFE-UHFFFAOYSA-N hydrogen peroxide;zinc Chemical compound [Zn].OO DLINORNFHVEIFE-UHFFFAOYSA-N 0.000 claims abstract description 4
- RVTZCBVAJQQJTK-UHFFFAOYSA-N oxygen(2-);zirconium(4+) Chemical compound [O-2].[O-2].[Zr+4] RVTZCBVAJQQJTK-UHFFFAOYSA-N 0.000 claims abstract description 4
- 239000000377 silicon dioxide Substances 0.000 claims abstract description 4
- 235000012239 silicon dioxide Nutrition 0.000 claims abstract description 4
- 239000000243 solution Substances 0.000 claims description 19
- PEDCQBHIVMGVHV-UHFFFAOYSA-N Glycerine Chemical compound OCC(O)CO PEDCQBHIVMGVHV-UHFFFAOYSA-N 0.000 claims description 12
- IXPNQXFRVYWDDI-UHFFFAOYSA-N 1-methyl-2,4-dioxo-1,3-diazinane-5-carboximidamide Chemical compound CN1CC(C(N)=N)C(=O)NC1=O IXPNQXFRVYWDDI-UHFFFAOYSA-N 0.000 claims description 9
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 claims description 9
- 235000010413 sodium alginate Nutrition 0.000 claims description 9
- 239000000661 sodium alginate Substances 0.000 claims description 9
- 229940005550 sodium alginate Drugs 0.000 claims description 9
- 239000012267 brine Substances 0.000 claims description 6
- HPALAKNZSZLMCH-UHFFFAOYSA-M sodium;chloride;hydrate Chemical compound O.[Na+].[Cl-] HPALAKNZSZLMCH-UHFFFAOYSA-M 0.000 claims description 6
- 229920002494 Zein Polymers 0.000 claims description 5
- 235000011187 glycerol Nutrition 0.000 claims description 5
- 239000013535 sea water Substances 0.000 claims description 5
- 239000005019 zein Substances 0.000 claims description 5
- 229940093612 zein Drugs 0.000 claims description 5
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 claims description 4
- 239000012460 protein solution Substances 0.000 claims description 4
- 238000003756 stirring Methods 0.000 claims description 4
- 239000008367 deionised water Substances 0.000 claims description 3
- 229910021641 deionized water Inorganic materials 0.000 claims description 3
- 239000000203 mixture Substances 0.000 claims description 3
- 239000004014 plasticizer Substances 0.000 claims description 3
- 238000006243 chemical reaction Methods 0.000 claims description 2
- 239000010793 electronic waste Substances 0.000 claims description 2
- 238000001132 ultrasonic dispersion Methods 0.000 claims 1
- 230000000694 effects Effects 0.000 abstract description 9
- GCICAPWZNUIIDV-UHFFFAOYSA-N lithium magnesium Chemical compound [Li].[Mg] GCICAPWZNUIIDV-UHFFFAOYSA-N 0.000 abstract description 2
- 240000008042 Zea mays Species 0.000 abstract 1
- 235000005824 Zea mays ssp. parviglumis Nutrition 0.000 abstract 1
- 235000002017 Zea mays subsp mays Nutrition 0.000 abstract 1
- 235000005822 corn Nutrition 0.000 abstract 1
- 229910052744 lithium Inorganic materials 0.000 description 24
- WHXSMMKQMYFTQS-UHFFFAOYSA-N Lithium Chemical compound [Li] WHXSMMKQMYFTQS-UHFFFAOYSA-N 0.000 description 22
- 229910010413 TiO 2 Inorganic materials 0.000 description 18
- 239000011777 magnesium Substances 0.000 description 11
- 238000010521 absorption reaction Methods 0.000 description 9
- 238000000926 separation method Methods 0.000 description 9
- -1 K + Chemical class 0.000 description 4
- 239000003463 adsorbent Substances 0.000 description 4
- 239000011734 sodium Substances 0.000 description 4
- FYYHWMGAXLPEAU-UHFFFAOYSA-N Magnesium Chemical compound [Mg] FYYHWMGAXLPEAU-UHFFFAOYSA-N 0.000 description 3
- 229910004298 SiO 2 Inorganic materials 0.000 description 3
- 238000002474 experimental method Methods 0.000 description 3
- 150000002500 ions Chemical class 0.000 description 3
- 229910052749 magnesium Inorganic materials 0.000 description 3
- 229910021645 metal ion Inorganic materials 0.000 description 3
- 229920000620 organic polymer Polymers 0.000 description 3
- 239000000843 powder Substances 0.000 description 3
- 238000011084 recovery Methods 0.000 description 3
- 229920006395 saturated elastomer Polymers 0.000 description 3
- 239000002253 acid Substances 0.000 description 2
- 150000001768 cations Chemical class 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 239000011148 porous material Substances 0.000 description 2
- 150000003839 salts Chemical class 0.000 description 2
- 238000001878 scanning electron micrograph Methods 0.000 description 2
- UXVMQQNJUSDDNG-UHFFFAOYSA-L Calcium chloride Chemical compound [Cl-].[Cl-].[Ca+2] UXVMQQNJUSDDNG-UHFFFAOYSA-L 0.000 description 1
- 229910019142 PO4 Inorganic materials 0.000 description 1
- 241000220317 Rosa Species 0.000 description 1
- AZDRQVAHHNSJOQ-UHFFFAOYSA-N alumane Chemical class [AlH3] AZDRQVAHHNSJOQ-UHFFFAOYSA-N 0.000 description 1
- 238000003321 atomic absorption spectrophotometry Methods 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 239000001110 calcium chloride Substances 0.000 description 1
- 229910001628 calcium chloride Inorganic materials 0.000 description 1
- 235000011148 calcium chloride Nutrition 0.000 description 1
- 238000005266 casting Methods 0.000 description 1
- 230000000052 comparative effect Effects 0.000 description 1
- 238000003795 desorption Methods 0.000 description 1
- 238000004090 dissolution Methods 0.000 description 1
- 238000010828 elution Methods 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 238000000605 extraction Methods 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 230000036571 hydration Effects 0.000 description 1
- 238000006703 hydration reaction Methods 0.000 description 1
- 229910052500 inorganic mineral Inorganic materials 0.000 description 1
- 238000011031 large-scale manufacturing process Methods 0.000 description 1
- 238000002386 leaching Methods 0.000 description 1
- XGZVUEUWXADBQD-UHFFFAOYSA-L lithium carbonate Chemical compound [Li+].[Li+].[O-]C([O-])=O XGZVUEUWXADBQD-UHFFFAOYSA-L 0.000 description 1
- 229910052808 lithium carbonate Inorganic materials 0.000 description 1
- 150000002696 manganese Chemical class 0.000 description 1
- 239000011159 matrix material Substances 0.000 description 1
- 238000009285 membrane fouling Methods 0.000 description 1
- 239000011707 mineral Substances 0.000 description 1
- 235000010755 mineral Nutrition 0.000 description 1
- 239000011259 mixed solution Substances 0.000 description 1
- 238000001728 nano-filtration Methods 0.000 description 1
- 230000035699 permeability Effects 0.000 description 1
- 239000010452 phosphate Substances 0.000 description 1
- NBIIXXVUZAFLBC-UHFFFAOYSA-K phosphate Chemical compound [O-]P([O-])([O-])=O NBIIXXVUZAFLBC-UHFFFAOYSA-K 0.000 description 1
- 229920000867 polyelectrolyte Polymers 0.000 description 1
- 229920005597 polymer membrane Polymers 0.000 description 1
- 229920001343 polytetrafluoroethylene Polymers 0.000 description 1
- 239000004810 polytetrafluoroethylene Substances 0.000 description 1
- 229910001414 potassium ion Inorganic materials 0.000 description 1
- 238000001556 precipitation Methods 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 238000004064 recycling Methods 0.000 description 1
- 230000008929 regeneration Effects 0.000 description 1
- 238000011069 regeneration method Methods 0.000 description 1
- 238000005185 salting out Methods 0.000 description 1
- 238000001338 self-assembly Methods 0.000 description 1
- 229910001415 sodium ion Inorganic materials 0.000 description 1
- 238000002336 sorption--desorption measurement Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 150000003608 titanium Chemical class 0.000 description 1
- OGIDPMRJRNCKJF-UHFFFAOYSA-N titanium oxide Inorganic materials [Ti]=O OGIDPMRJRNCKJF-UHFFFAOYSA-N 0.000 description 1
- 238000002525 ultrasonication Methods 0.000 description 1
Images
Classifications
-
- 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
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P10/00—Technologies related to metal processing
- Y02P10/20—Recycling
Landscapes
- Solid-Sorbent Or Filter-Aiding Compositions (AREA)
Abstract
Description
技术领域technical field
本发明属于锂离子的吸附分离技术领域,具体涉及一种基于蛋白质/无机纳米颗粒复合膜从液态水环境中选择性吸附锂离子的方法。The invention belongs to the technical field of adsorption and separation of lithium ions, and in particular relates to a method for selectively adsorbing lithium ions from a liquid water environment based on a protein/inorganic nanoparticle composite membrane.
背景技术Background technique
全球总的可开采锂储量约1400万吨(以锂金属计),超过60%的锂资源在盐湖卤水中。与矿物和矿石相比,从经济和环境效益两方面来说,从液态锂资源中提取锂更便宜、更容易。我国锂资源储量丰富,主要分布于青海和西藏地区的盐湖中,约占我国锂资源总储量的80%,占世界锂资源总储量的1/3。国外大多数盐湖镁锂比低,利用沉淀法已实现碳酸锂产品的规模化生产。而我国盐湖卤水普遍存在高镁锂比特性(>30),由于镁锂化学性质相似且离子水合半径相差较小,使得镁锂分离的难度大大增加。此外,盐湖卤水中还有许多共存离子(例如K+、Mg2+、Ca2+、Cl-、SO4 2-等),使得锂离子的分离更为困难。因此,迫切需要开发和完善从低品位卤水中高效分离Li+的技术。The total recoverable lithium reserves in the world are about 14 million tons (calculated as lithium metal), and more than 60% of lithium resources are in salt lake brine. Compared with minerals and ores, it is cheaper and easier to extract lithium from liquid lithium resources in terms of both economic and environmental benefits. my country's lithium resources are rich in reserves, mainly distributed in the salt lakes of Qinghai and Tibet, accounting for about 80% of my country's total lithium resources reserves, accounting for 1/3 of the world's total lithium resources reserves. Most foreign salt lakes have a low ratio of magnesium to lithium, and the large-scale production of lithium carbonate products has been realized by the precipitation method. However, salt lake brine in my country generally has a high magnesium-lithium ratio (>30). Due to the similar chemical properties of magnesium and lithium and the small difference in ion hydration radius, the difficulty of separating magnesium and lithium is greatly increased. In addition, there are many coexisting ions (such as K + , Mg 2+ , Ca 2+ , Cl - , SO 4 2- , etc.) in salt lake brine, which makes the separation of lithium ions more difficult. Therefore, there is an urgent need to develop and perfect technologies for efficient separation of Li + from low-grade brines.
膜技术因其固有的低能耗和高分离效率而被认为是回收锂的一种有前景的分离方法。许多研究报道了通过聚电解质多层自组装制备的纳滤膜可从盐水中提取Li+,但盐析造成的膜污染会大大降低其选择性和渗透性。锂离子筛(如锰系、钛系、锑酸盐、铝盐和磷酸盐型等)具有较大的吸附量和高的Li+选择性,但粉末状锂离子筛吸附剂在过滤回收过程中损失较大,并且酸洗脱附时的溶解损耗也较大。为了解决上述问题,一些研究将锂离子筛插入聚合物膜基质中,制备具有吸附锂离子功能的吸附膜。这类吸附膜结合了吸附和膜分离的优点,在一定程度上提高了锂离子的回收效率。然而,在铸膜过程中,由于有机聚合物溶液进入到锂离子筛吸附剂的孔隙内部,会堵塞吸附剂孔道,并且有机聚合物的疏水性会导致锂离子筛吸附容量比粉末原料吸附容量降低20%~50%。Membrane technology has been considered as a promising separation method for lithium recovery due to its inherent low energy consumption and high separation efficiency. Many studies have reported that nanofiltration membranes prepared by polyelectrolyte multilayer self-assembly can extract Li + from brine, but the membrane fouling caused by salting out will greatly reduce its selectivity and permeability. Lithium ion sieves (such as manganese series, titanium series, antimonate, aluminum salt and phosphate type, etc.) have large adsorption capacity and high Li + selectivity, but the powdered lithium ion sieve adsorbent is difficult to obtain in the process of filtration and recovery. The loss is large, and the dissolution loss during acid elution and desorption is also large. In order to solve the above problems, some studies have inserted lithium ion sieves into polymer membrane matrix to prepare adsorption membranes with the function of adsorbing lithium ions. This type of adsorption membrane combines the advantages of adsorption and membrane separation, and improves the recovery efficiency of lithium ions to a certain extent. However, during the film casting process, since the organic polymer solution enters the pores of the lithium-ion sieve adsorbent, the pores of the adsorbent will be blocked, and the hydrophobicity of the organic polymer will cause the adsorption capacity of the lithium-ion sieve to decrease compared with that of the powder raw material. 20% to 50%.
发明内容Contents of the invention
本发明的目的是克服现有吸附膜分离锂离子存在的问题,提供一种基于蛋白质/无机纳米颗粒复合膜选择性吸附锂离子的方法,该方法对锂离子的吸附容量高、吸附选择性高、再生性能好。The purpose of the present invention is to overcome the problems existing in the separation of lithium ions by existing adsorption membranes, and provide a method for selectively adsorbing lithium ions based on protein/inorganic nanoparticle composite membranes, which has high adsorption capacity and high adsorption selectivity for lithium ions , Good regeneration performance.
针对上述目的,本发明采用的技术方案是以蛋白质/无机纳米颗粒复合膜为吸附材料,在pH为5~9的条件下从液态水中选择性吸附锂离子;其中,所述蛋白质为大豆分离蛋白或玉米蛋白,所述无机纳米颗粒为二氧化钛、二氧化锆、二氧化锰、二氧化硅、二氧化锌中任意一种;优选蛋白质为大豆分离蛋白,无机纳米颗粒为二氧化钛。所述液态水是盐湖卤水、海水、电子废弃物(如锂离子电池)浸取液中任意一种。For the above-mentioned purpose, the technical solution adopted in the present invention is to use the protein/inorganic nanoparticle composite membrane as the adsorption material to selectively adsorb lithium ions from liquid water under the condition of pH 5-9; wherein, the protein is soybean protein isolate Or zein, the inorganic nanoparticles are any one of titanium dioxide, zirconium dioxide, manganese dioxide, silicon dioxide, zinc dioxide; preferably the protein is soybean protein isolate, and the inorganic nanoparticles are titanium dioxide. The liquid water is any one of salt lake brine, seawater, and electronic waste (such as lithium ion battery) leaching solution.
上述蛋白质/无机纳米颗粒复合膜的制备方法为:将蛋白质完全溶解于0.05~1mol/LNaOH水溶液中,形成蛋白质溶液;然后在蛋白质溶液中加入海藻酸钠和无机纳米颗粒,超声分散均匀,再加入甘油作为增塑剂,搅拌6~12小时后,将混合物倒入模具中干燥成膜,再将模具置于CaCl2水溶液中,在室温下交联12~24小时,反应结束后,用乙醇将膜从模具中剥离,用去离子水洗涤后干燥,即得到蛋白质/无机纳米颗粒复合膜。The preparation method of the above-mentioned protein/inorganic nanoparticle composite film is as follows: completely dissolve the protein in 0.05-1mol/L NaOH aqueous solution to form a protein solution; then add sodium alginate and inorganic nanoparticles to the protein solution, ultrasonically disperse evenly, and then add Glycerin is used as a plasticizer, after stirring for 6-12 hours, pour the mixture into a mold to dry to form a film, then place the mold in CaCl 2 aqueous solution, and cross-link at room temperature for 12-24 hours. The membrane was peeled off from the mold, washed with deionized water and dried to obtain a protein/inorganic nanoparticle composite membrane.
上述述蛋白质/无机纳米颗粒复合膜的制备方法中,所述蛋白质与海藻酸钠、无机纳米颗粒的质量比为20~100:1:1~6;所述甘油的加入量与蛋白质的比1mL:20~400mg;所述CaCl2水溶液的浓度为0.5~4mg/mL。In the preparation method of the above-mentioned protein/inorganic nanoparticle composite film, the mass ratio of the protein to sodium alginate and the inorganic nanoparticle is 20-100:1:1-6; the ratio of the added amount of the glycerol to the protein is 1mL : 20~400mg; Described CaCl The concentration of aqueous solution is 0.5~4mg/mL.
本发明基于蛋白质/无机纳米颗粒复合膜选择性吸附锂离子的具体方法为:将蛋白质/无机纳米颗粒加入液态水中,调节pH为5~9,置于振荡器中震荡1~2小时,进行锂离子吸附。进一步可将蛋白质/无机纳米颗粒复合膜吸附锂离子后置于0.5~1mol/L HCl水溶液中,震荡10~12小时,解吸吸附的锂离子后,蛋白质/无机纳米颗粒复合膜重复用于吸附锂离子。其中,所述蛋白质/无机纳米颗粒复合膜与液态水的固液比为0.5~5g/L。The specific method for the selective adsorption of lithium ions based on the protein/inorganic nanoparticle composite film of the present invention is as follows: adding the protein/inorganic nanoparticle into liquid water, adjusting the pH to 5-9, placing it in an oscillator for 1-2 hours, and performing lithium ion ion adsorption. Further, the protein/inorganic nanoparticle composite membrane can be placed in 0.5-1mol/L HCl aqueous solution after adsorbing lithium ions, and shaken for 10-12 hours. After desorbing the adsorbed lithium ions, the protein/inorganic nanoparticle composite membrane can be reused to adsorb lithium ion. Wherein, the solid-to-liquid ratio of the protein/inorganic nanoparticle composite membrane to liquid water is 0.5-5 g/L.
本发明的有益效果如下:The beneficial effects of the present invention are as follows:
1)相较于粉末状的锂离子吸附剂,本发明将无机纳米颗粒负载到蛋白质膜中,可以较好的将无机纳米颗粒分散在膜中,并且吸附后便于回收利用。1) Compared with the powdered lithium ion adsorbent, the present invention loads the inorganic nanoparticles into the protein film, can better disperse the inorganic nanoparticles in the film, and facilitates recycling after adsorption.
2)相较于有机聚合物膜基分离材料,本发明蛋白质膜材料对环境无污染,耐酸、不影响无机纳米颗粒对锂离子的吸附量,且蛋白质含有大量活性基团,具有可再生、可生物降解性等优点。2) Compared with the organic polymer membrane-based separation material, the protein membrane material of the present invention has no pollution to the environment, is acid-resistant, does not affect the adsorption capacity of inorganic nanoparticles to lithium ions, and contains a large number of active groups in the protein, which is renewable and reproducible. advantages of biodegradability.
3)本发明蛋白质膜材料的制备方法简单,成本低廉,能够快速选择性地从高镁锂比水溶液中提取锂离子,经济实用,操作简便,具有较好的推广应用前景。3) The preparation method of the protein membrane material of the present invention is simple and low in cost, and can quickly and selectively extract lithium ions from an aqueous solution with a high magnesium-to-lithium ratio.
附图说明Description of drawings
图1是实施例1中SPI/TiO2复合膜的扫描电镜图。Fig. 1 is the scanning electron micrograph of SPI/TiO 2 composite film in
图2是pH对SPI/TiO2复合膜吸附性能的影响。Figure 2 shows the effect of pH on the adsorption performance of SPI/TiO 2 composite membranes.
图3是锂离子浓度对SPI/TiO2复合膜吸附性能的影响。Figure 3 is the effect of lithium ion concentration on the adsorption performance of SPI/TiO 2 composite film.
图4是吸附时间对SPI/TiO2复合膜吸附性能的影响。Figure 4 is the effect of adsorption time on the adsorption performance of SPI/TiO 2 composite membranes.
图5是SPI/TiO2复合膜在混合金属离子溶液中对锂的吸附。Figure 5 shows the adsorption of lithium by the SPI/ TiO2 composite film in the mixed metal ion solution.
图6是SPI/TiO2复合膜对模拟海水中锂离子的吸附。Figure 6 shows the adsorption of lithium ions in simulated seawater by the SPI/TiO 2 composite membrane.
图7是SPI/TiO2复合膜对锂离子的解吸-吸附。Figure 7 shows the desorption-adsorption of lithium ions by the SPI/TiO 2 composite film.
具体实施方式Detailed ways
下面结合附图和实施例对本发明进一步详细说明,但本发明的保护范围不仅限于这些实施例。The present invention will be described in further detail below in conjunction with the accompanying drawings and embodiments, but the protection scope of the present invention is not limited to these embodiments.
实施例1Example 1
将200mg大豆分离蛋白(SPI)加入到5mL 0.1mol/L NaOH水溶液中,搅拌至蛋白完全溶解形成大豆分离蛋白溶液。然后在大豆分离蛋白溶液中加10mg海藻酸钠(SA)和20mg二氧化钛,超声30分钟使其分散均匀,再加入0.5mL甘油作为增塑剂,搅拌分散6小时后,将混合物倒入直径为50mm的聚四氟乙烯模具中,放入80℃烘箱中干燥成膜。最后,将膜具置于5mL 2mg/mL CaCl2水溶液中,并在室温下交联12小时。反应结束后,用乙醇将膜从模具中剥离,用去离子水洗涤膜5次后干燥,得到SPI/TiO2复合膜。从图1的扫描电镜图可以看出,TiO2纳米颗粒被包覆在SPI膜中。Add 200 mg of soybean protein isolate (SPI) into 5 mL of 0.1 mol/L NaOH aqueous solution, and stir until the protein is completely dissolved to form a soybean protein isolate solution. Then add 10mg sodium alginate (SA) and 20mg titanium dioxide to the soybean protein isolate solution, and disperse it evenly by ultrasonication for 30 minutes, then add 0.5mL glycerin as a plasticizer, stir and disperse for 6 hours, and pour the mixture into Put it into a polytetrafluoroethylene mold and dry it in an oven at 80°C to form a film. Finally, the membrane was placed in 5 mL of 2 mg/mL CaCl2 aqueous solution and crosslinked at room temperature for 12 h. After the reaction, the membrane was peeled off from the mold with ethanol, washed with deionized water for 5 times and then dried to obtain the SPI/ TiO2 composite membrane. It can be seen from the SEM image of Fig. 1 that the TiO2 nanoparticles are coated in the SPI film.
采用上述SPI/TiO2复合膜分别下不同条件下吸附锂离子,具体实验如下:The above-mentioned SPI/TiO 2 composite film was used to adsorb lithium ions under different conditions, and the specific experiments were as follows:
1、pH对复合膜吸附性能的影响1. The effect of pH on the adsorption performance of the composite membrane
分别将10mL 20mg/L Li+水溶液的pH值调节为2.3、3.9、5.1、6.7、8.4、9.8,然后加入SPI/TiO2复合膜(1cm×1cm,13mg),置于振荡器中震荡2小时后用原子吸收分光光度计测溶液中所含锂离子的含量。图2结果显示,该吸附材料在pH为5~9的范围对锂的吸附率达到85%以上。Adjust the pH value of 10mL 20mg/L Li + aqueous solution to 2.3, 3.9, 5.1, 6.7, 8.4, 9.8 respectively, then add SPI/TiO2 composite membrane (1cm×1cm, 13mg) and shake in a shaker for 2 hours Finally, the content of lithium ions contained in the solution was measured with an atomic absorption spectrophotometer. The results shown in Fig. 2 show that the adsorption rate of the adsorption material to lithium reaches more than 85% in the pH range of 5-9.
2、锂离子浓度对复合膜吸附性能的影响2. The effect of lithium ion concentration on the adsorption performance of the composite membrane
分别将10mL 2~100mg/L Li+水溶液的pH值调节为7,然后加入SPI/TiO2复合膜(1cm×1cm,13mg),考察在室温下对锂离子的吸附,置于振荡器中震荡2小时后,用原子吸收分光光度计测溶液中所含锂离子的含量。图3结果显示,随着浓度的升高锂的吸附量增加,该膜对锂的最大饱和吸附量为24.4mg/g。Adjust the pH value of
3、吸附时间对复合膜吸附性能的影响3. Effect of adsorption time on adsorption performance of composite membrane
将10mL 50mg/L Li+水溶液的pH值调节为7,然后加入SPI/TiO2复合膜(1cm×1cm,13mg),考察在不同时间复合膜对锂离子的吸附,用原子吸收分光光度计测溶液中所含锂离子的含量。图4结果显示,该膜对锂离子的吸附量在前1小时内急剧上升至22.3mg/g,在2小时内缓慢上升并达到平衡。The pH value of 10mL 50mg/L Li + aqueous solution was adjusted to 7, and then SPI/ TiO2 composite membrane (1cm×1cm, 13mg) was added to investigate the adsorption of lithium ions by the composite membrane at different times, using an atomic absorption spectrophotometer The content of lithium ions contained in the solution. The results shown in Figure 4 show that the adsorption capacity of the membrane for lithium ions rose sharply to 22.3 mg/g in the first 1 hour, then rose slowly and reached equilibrium within 2 hours.
4、SPI/TiO2复合膜在混合金属离子溶液中对锂的吸附4. Adsorption of Lithium by SPI/TiO 2 Composite Membrane in Mixed Metal Ion Solution
配制含有Mg2+、Ca2+、Na+、K+和Li+的金属离子混合溶液,其中Mg2+、Ca2+、Na+、K+离子的浓度均为1ppm或均为10ppm或均为50ppm,Li+离子的浓度均为1ppm,并调节pH值为7,加入SPI/TiO2复合膜(1cm×1cm,13mg),置于振荡器中震荡2小时后,用原子吸收分光光度计测溶液中所含锂离子的含量。图5结果显示,当Mg/Li比为10和50时,获得的分离因子值α分别高达600和1000,这表明Li+与其他阳离子共存时,阳离子(Mg2+、Ca2+、Na+和K+)的存在对Li+吸附没有显著影响,说明SPI/TiO2复合膜在Mg2+/Li+比值相对较高的情况下,对Li+具有较高的选择性。Prepare a mixed solution of metal ions containing Mg 2+ , Ca 2+ , Na + , K + and Li + , in which the concentrations of Mg 2+ , Ca 2+ , Na + , and K + ions are all 1ppm or 10ppm or all 50ppm, the concentration of Li + ions is 1ppm, and adjust the pH value to 7, add SPI/TiO 2 composite film (1cm × 1cm, 13mg), place it in an oscillator for 2 hours, and use an atomic absorption spectrophotometer Measure the content of lithium ions in the solution. The results in Fig. 5 show that when the Mg/Li ratio is 10 and 50, the obtained separation factor values α are as high as 600 and 1000, respectively, which indicates that when Li + coexists with other cations, the cations (Mg 2+ , Ca 2+ , Na + and K + ) had no significant effect on Li + adsorption, indicating that the SPI/TiO 2 composite membrane had a high selectivity for Li + at a relatively high Mg 2+ /Li + ratio.
5、SPI/TiO2复合膜在模拟海水中对锂的选择性提取5. Selective extraction of lithium by SPI/TiO 2 composite membrane in simulated seawater
配制含有1144ppm Mg2+、457ppm Ca2+、10770ppm Na+、332ppm K+和0.21ppm Li+的模拟海水,并调节pH值为7,加入SPI/TiO2复合膜(1cm×1cm,13mg),置于振荡器中震荡2小时后,用原子吸收分光光度计测溶液中所含锂离子的含量。图6结果表明,在高的离子浓度(1144ppm Mg2+、457ppm Ca2+、10770ppm Na+、332ppmK+)下,该复合膜对于低浓度的锂离子具有较好的吸附效果,锂离子的吸附率可达到85%。Prepare simulated seawater containing 1144ppm Mg 2+ , 457ppm Ca 2+ , 10770ppm Na + , 332ppm K + and 0.21ppm Li + , and adjust the pH value to 7, add SPI/TiO 2 composite membrane (1cm×1cm, 13mg), After shaking in an oscillator for 2 hours, use an atomic absorption spectrophotometer to measure the content of lithium ions contained in the solution. The results in Figure 6 show that the composite membrane has a good adsorption effect on low-concentration lithium ions at high ion concentrations (1144ppm Mg 2+ , 457ppm Ca 2+ , 10770ppm Na + , 332ppmK + ), and the adsorption of lithium ions The rate can reach 85%.
6、SPI/TiO2复合膜对锂离子的解吸-吸附实验6. Desorption-adsorption experiment of SPI/TiO 2 composite film for lithium ions
将SPI/TiO2复合膜(1cm×1cm,13mg)加入到10mL pH值为7的20mg/L Li+水溶液中,置于振荡器中震荡2小时后,将吸附锂离子后的复合膜加入到50mL 0.5mol/L HCl水溶液中,缓慢震荡12小时,用原子吸收分光光度计测溶液中所含锂离子的含量。对解吸后的复合膜再次进行吸附实验,解吸-吸附重复四次。结果显示进行四次吸附-脱附后,锂的吸附率仍可达到90%(见图7)。Add the SPI/ TiO2 composite membrane (1cm×1cm, 13mg) into 10mL of 20mg/L Li + aqueous solution with a pH value of 7, place it in a shaker for 2 hours, and add the composite membrane after absorbing lithium ions to the In 50mL 0.5mol/L HCl aqueous solution, shake slowly for 12 hours, and use an atomic absorption spectrophotometer to measure the content of lithium ions contained in the solution. The adsorption experiment was carried out again on the desorbed composite membrane, and the desorption-adsorption was repeated four times. The results show that after four adsorption-desorption, the adsorption rate of lithium can still reach 90% (see Figure 7).
实施例2Example 2
本实施例中用等质量玉米蛋白替换实施例1的大豆分离蛋白,其他步骤与实施例1相同,得到玉米蛋白/TiO2复合膜。In this embodiment, the soybean protein isolate of Example 1 was replaced with equal mass zein, and other steps were the same as in Example 1 to obtain zein/TiO Composite film.
分别将10mL 2、10、20、50、100mg/L Li+水溶液的pH值调节为7,然后加入玉米蛋白/TiO2复合膜(1cm×1cm,16mg),考察在室温下对锂离子的吸附,置于振荡器中震荡2小时后,用原子吸收分光光度计测溶液中所含锂离子的含量。结果显示,随着浓度的升高锂的吸附量增加,该膜对锂的最大饱和吸附量为27.2mg/g。The pH value of
实施例3Example 3
本实施例中用等质量二氧化锆替换实施例1的二氧化钛,其他步骤与实施例1相同,得到SPI/ZrO2复合膜。In this example, the titanium dioxide in Example 1 was replaced with zirconium dioxide of equal mass, and the other steps were the same as in Example 1 to obtain the SPI/ZrO 2 composite film.
分别将10mL 2、10、20、50、100mg/L Li+水溶液的pH值调节为7,然后加入实施例3中SPI/ZrO2复合膜(1cm×1cm,14.5mg),考察在室温下对锂离子的吸附,置于振荡器中震荡2小时后,用原子吸收分光光度计测溶液中所含锂离子的含量。结果显示,随着浓度的升高锂的吸附量增加,该膜对锂的最大饱和吸附量为20.1mg/g。The pH value of the
实施例4Example 4
本实施例中用等质量二氧化锰、二氧化硅、二氧化锌分别替换实施例1的二氧化钛,其他步骤与实施例1相同,分别得到SPI/MnO2、SPI/SiO2以及SPI/ZnO2复合膜。In this example, manganese dioxide, silicon dioxide, and zinc dioxide were used to replace the titanium dioxide in Example 1, and the other steps were the same as in Example 1 to obtain SPI/MnO 2 , SPI/SiO 2 , and SPI/ZnO 2 . Composite film.
分别将SPI/MnO2(1cm×1cm,12mg)、SPI/SiO2(1cm×1cm,12mg)以及SPI/ZnO2(1cm×1cm,12mg)复合膜加入到10mL pH值为7的5mg/L Li+水溶液中,置于振荡器中震荡2小时后,用原子吸收分光光度计测溶液中所含锂离子的含量。结果显示,SPI/MnO2、SPI/SiO2以及SPI/ZnO2复合膜对锂离子的吸附率分别为79.3%、68.1%、61.2%。SPI/MnO 2 (1cm×1cm, 12mg), SPI/SiO 2 (1cm×1cm, 12mg) and SPI/ZnO 2 (1cm×1cm, 12mg) composite membranes were added to 10mL of 5mg/L In the Li + aqueous solution, after being placed in a shaker to vibrate for 2 hours, the content of lithium ions contained in the solution was measured with an atomic absorption spectrophotometer. The results showed that the adsorption rates of lithium ions for SPI/MnO 2 , SPI/SiO 2 and SPI/ZnO 2 composite films were 79.3%, 68.1%, and 61.2%, respectively.
对比例1Comparative example 1
在实施例1中仅不加二氧化钛,其他步骤与实施例1相同,得到SPI/SA复合膜。In Example 1, titanium dioxide was not added, and other steps were the same as in Example 1 to obtain an SPI/SA composite film.
分别将10mg SPI/TiO2复合膜、SPI/SA复合膜以及TiO2粉末加入到10mL pH值为7的2mg/L Li+水溶液中,置于振荡器中震荡2小时后,用原子吸收分光光度计测溶液中所含锂离子的含量。结果显示,SPI/TiO2复合膜、SPI/SA复合膜以及TiO2粉末对锂离子的吸附率分别为92.3%、2.1%、78.4%。Add 10 mg of SPI/TiO 2 composite film, SPI/SA composite film and TiO 2 powder into 10 mL of 2 mg/L Li + aqueous solution with a pH value of 7, place them in a shaker for 2 hours, and use atomic absorption spectrophotometry The content of lithium ions contained in the solution was measured. The results showed that the adsorption rates of SPI/TiO 2 composite film, SPI/SA composite film and TiO 2 powder to lithium ions were 92.3%, 2.1%, and 78.4%, respectively.
Claims (8)
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN202211509531.4A CN115715976A (en) | 2022-11-29 | 2022-11-29 | Selective Lithium Ion Adsorption Method Based on Protein/Inorganic Nanoparticle Composite Membrane |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN202211509531.4A CN115715976A (en) | 2022-11-29 | 2022-11-29 | Selective Lithium Ion Adsorption Method Based on Protein/Inorganic Nanoparticle Composite Membrane |
Publications (1)
Publication Number | Publication Date |
---|---|
CN115715976A true CN115715976A (en) | 2023-02-28 |
Family
ID=85256873
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN202211509531.4A Pending CN115715976A (en) | 2022-11-29 | 2022-11-29 | Selective Lithium Ion Adsorption Method Based on Protein/Inorganic Nanoparticle Composite Membrane |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN115715976A (en) |
Citations (11)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4190576A (en) * | 1975-11-26 | 1980-02-26 | United Kingdom Atomic Energy Authority | Separation of macromolecules |
CN105214624A (en) * | 2015-11-02 | 2016-01-06 | 李建中 | A kind of dislysate adsorption stuffing, its preparation method and application |
CN106902745A (en) * | 2017-03-08 | 2017-06-30 | 江苏大学 | A kind of preparation method and applications of lithium/rubidium ion synchronization adsorbent |
CN107837791A (en) * | 2017-12-06 | 2018-03-27 | 西南交通大学 | A kind of PEI modified celluloses membrane adsorbent and preparation method thereof |
CN107899551A (en) * | 2017-10-11 | 2018-04-13 | 福建鸿燕化工有限公司 | Amino group graphene/cellulose acetate composite material and its application containing polypyrrole |
CN107930594A (en) * | 2017-11-20 | 2018-04-20 | 成都新柯力化工科技有限公司 | A kind of modification egg film paper and preparation method and application for lithium battery recycling |
US20180353907A1 (en) * | 2015-06-24 | 2018-12-13 | Albemarle Corporation | Purification of Lithium-Containing Brine |
CN109632922A (en) * | 2019-01-17 | 2019-04-16 | 天津工业大学 | A preparation method of molecularly imprinted hydrogel modified electrode that can recognize proteins |
CN112316928A (en) * | 2020-10-19 | 2021-02-05 | 邢台职业技术学院 | Cellulose lithium ion sieve composite membrane and preparation method and application thereof |
CN113522061A (en) * | 2021-07-21 | 2021-10-22 | 昆明理工大学 | Preparation method of high-adsorption-capacity lithium ion imprinting nano composite membrane |
CN115160650A (en) * | 2022-06-08 | 2022-10-11 | 中国热带农业科学院农产品加工研究所 | A kind of TiO2 cellulose nanocomposite film and preparation method thereof |
-
2022
- 2022-11-29 CN CN202211509531.4A patent/CN115715976A/en active Pending
Patent Citations (11)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4190576A (en) * | 1975-11-26 | 1980-02-26 | United Kingdom Atomic Energy Authority | Separation of macromolecules |
US20180353907A1 (en) * | 2015-06-24 | 2018-12-13 | Albemarle Corporation | Purification of Lithium-Containing Brine |
CN105214624A (en) * | 2015-11-02 | 2016-01-06 | 李建中 | A kind of dislysate adsorption stuffing, its preparation method and application |
CN106902745A (en) * | 2017-03-08 | 2017-06-30 | 江苏大学 | A kind of preparation method and applications of lithium/rubidium ion synchronization adsorbent |
CN107899551A (en) * | 2017-10-11 | 2018-04-13 | 福建鸿燕化工有限公司 | Amino group graphene/cellulose acetate composite material and its application containing polypyrrole |
CN107930594A (en) * | 2017-11-20 | 2018-04-20 | 成都新柯力化工科技有限公司 | A kind of modification egg film paper and preparation method and application for lithium battery recycling |
CN107837791A (en) * | 2017-12-06 | 2018-03-27 | 西南交通大学 | A kind of PEI modified celluloses membrane adsorbent and preparation method thereof |
CN109632922A (en) * | 2019-01-17 | 2019-04-16 | 天津工业大学 | A preparation method of molecularly imprinted hydrogel modified electrode that can recognize proteins |
CN112316928A (en) * | 2020-10-19 | 2021-02-05 | 邢台职业技术学院 | Cellulose lithium ion sieve composite membrane and preparation method and application thereof |
CN113522061A (en) * | 2021-07-21 | 2021-10-22 | 昆明理工大学 | Preparation method of high-adsorption-capacity lithium ion imprinting nano composite membrane |
CN115160650A (en) * | 2022-06-08 | 2022-10-11 | 中国热带农业科学院农产品加工研究所 | A kind of TiO2 cellulose nanocomposite film and preparation method thereof |
Non-Patent Citations (5)
Title |
---|
FACUI YANG ET AL.: "Isolated Soy Protein/TiO2 Membrane Adsorber for Selective Separation of Lithium Ion", 《SSRN ELECTRONIC JOURNAL》, pages 2 * |
JING YU ET AL.: "Calcium ion-sodium alginate double cross-linked graphene oxide nanofiltration membrane with enhanced stability for efficient separation of dyes", 《SEPARATION AND PURIFICATION TECHNOLOGY》, vol. 276, pages 119348 * |
王盼: "锂离子筛膜的制备及其吸附性能研究", 《中国优秀硕士学位论文全文数据库 工程科技Ⅰ辑》, no. 3 * |
王蕾等: "聚氯乙烯锂离子筛膜的制备及其在卤水中的 锂吸附性能", 《复合材料学报》, vol. 40, no. 9, pages 5107 - 5123 * |
贾祥祥: "制备条件对玉米醇溶蛋白膜性能的影响研究", 《中国优秀硕士学位论文全文数据库 工程科技Ⅰ辑》, no. 2, pages 26 - 27 * |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN101733074B (en) | Method for preparing film type biological adsorbing medium | |
CN107824163B (en) | A kind of MIL-125(Ti)/chitosan composite microspheres adsorbing arsenic | |
CN102029144A (en) | Adsorbent for adsorbing heavy metal ions and dye in waste water and preparation method thereof | |
CN108543516B (en) | Lithium ion selective adsorbent, preparation method and process for extracting lithium from brine | |
CN108479719B (en) | High-performance ion exchange type adsorbent, preparation and application for extracting rubidium/lithium | |
WO2020238505A1 (en) | Adsorption material based on crosslinked protein, and application thereof for recovering precious metals | |
CN108355621B (en) | Magnetic porous bentonite chitosan composite microsphere and preparation method thereof | |
CN108262025A (en) | The preparation method of porous nano composite material and its application in removal of heavy metal ions | |
Zhang et al. | Preparation of novel poly (sodium p-styrenesulfonate)/sodium alginate hydrogel incorporated with MOF-5 nanoparticles for the adsorption of Pb (II) and tetracycline | |
CN107158979A (en) | A kind of preparation method and its usage of lithium ion trace hybridized film | |
Li et al. | Efficient recovery of lithium from spent lithium-ion battery raffinate by Mn and Al-based adsorbents: pretreatment, adsorption mechanism, and performance comparison | |
CN104307492A (en) | A kind of Mg2Al-LS-LDH composite material and its preparation method and application | |
CN112316895B (en) | Composite material for selectively removing aluminum ions in rare earth ion solution and preparation method thereof | |
CN110038535B (en) | Regeneration method of polyvinylidene fluoride separation membrane carrying thiourea groups and used for adsorbing silver ions | |
CN102352448B (en) | Method for recovering rare earth from low-concentration rare earth solution through prussian blue colloidal nanoparticles | |
CN115715976A (en) | Selective Lithium Ion Adsorption Method Based on Protein/Inorganic Nanoparticle Composite Membrane | |
CN112973618A (en) | Layered metal sulfide adsorbent, preparation method thereof and method for selectively enriching lead ions from heavy metal wastewater | |
CN113559825A (en) | Preparation method, product and application of ZIF-8/sodium bentonite composite material | |
CN108428486B (en) | Cesium ion removal method based on bentonite chitosan composite microspheres | |
CN102886241B (en) | Preparation method of diatomite heavy-metal adsorption material | |
CN105944656A (en) | Titanium-based heavy metal ion adsorbent as well as preparation method and application thereof | |
JP3646156B2 (en) | Film-like lithium adsorbing material, method for producing the same, and method for recovering lithium using the same | |
CN116139832A (en) | Preparation and application of zeolite immobilized hydrogel beads | |
CN115634670B (en) | PEI modified sodium alginate loaded clay mineral gel microsphere and preparation method and application thereof | |
CN113044938B (en) | Functionalized two-dimensional layered MXene membranes for the treatment of toxic ions in wastewater |
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 | ||
WD01 | Invention patent application deemed withdrawn after publication | ||
WD01 | Invention patent application deemed withdrawn after publication |
Application publication date: 20230228 |