WO2022134221A1 - 一种多孔纺丝复合材料的制备方法及其提锂应用 - Google Patents

一种多孔纺丝复合材料的制备方法及其提锂应用 Download PDF

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WO2022134221A1
WO2022134221A1 PCT/CN2021/070555 CN2021070555W WO2022134221A1 WO 2022134221 A1 WO2022134221 A1 WO 2022134221A1 CN 2021070555 W CN2021070555 W CN 2021070555W WO 2022134221 A1 WO2022134221 A1 WO 2022134221A1
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lithium
spinning
porous
adsorption
composite
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French (fr)
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邓天龙
赵凯宇
余晓平
李明礼
多吉
郭亚飞
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Central Laboratory Of Geological Mineral Exploration And Development Bureau Of Tibet Autonomous Region
Tianjin University of Science and Technology
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Central Laboratory Of Geological Mineral Exploration And Development Bureau Of Tibet Autonomous Region
Tianjin University of Science and Technology
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    • C22B26/00—Obtaining alkali, alkaline earth metals or magnesium
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Definitions

  • the invention belongs to the field of material chemical industry, and relates to a lithium ion adsorption material, in particular to a method for a porous spinning composite material.
  • Lithium as the lightest metal, is widely used in aerospace, lithium-ion batteries, nuclear industry, ceramics, electronic devices and other fields, and is known as the "strategic energy metal" in the 21st century. With the continuous development of modern high-tech, people's demand for lithium is increasing day by day.
  • the sources of lithium are mainly divided into two categories: one is solid lithium ore resources mainly composed of lepidolite, spodumene, and feldspar; the other is mainly salt lake brine, concentrated seawater, geothermal water, underground brine, etc. of liquid lithium ore resources.
  • solid lithium ore resources mainly composed of lepidolite, spodumene, and feldspar
  • the other is mainly salt lake brine, concentrated seawater, geothermal water, underground brine, etc.
  • the methods of extracting lithium from liquid lithium ore mainly include precipitation method, electrochemical method, extraction method, adsorption method, etc.
  • the adsorption method has the advantages of low cost, simple process, green and high efficiency, and has gradually become the most promising extraction method.
  • Lithium method The key to this technology is the preparation of lithium adsorbents with excellent adsorption performance, and lithium ion sieve oxides have gradually become a research hotspot because of their high adsorption capacity and lithium ion selectivity.
  • most of the lithium ion sieve oxides exist in the form of ultrafine powder, and the poor fluidity and cycle stability greatly limit their industrial application.
  • the key to solving this problem is to prepare a kind of high adsorption capacity, adsorption A composite lithium ion sieve adsorbent with fast rate, good cycle stability and low cost.
  • Patent CN101898113A discloses a spherical lithium ion with polyvinyl chloride as binder and manganese-based lithium ion sieve (LMO: LiMn 2 O 4 , Li 1.6 Mn 1.6 O 4 , Li 4 Mn 5 O 12 ) as the core material
  • LMO manganese-based lithium ion sieve
  • the ion composite adsorbent although the problem of poor fluidity has been improved, the adsorption rate of the coated lithium ion sieve drops significantly.
  • Patent CN106902781B discloses a HMO-loaded mesoporous hollow silicon sphere, which has a large specific surface area and adsorption rate, but the lithium ion sieve is directly exposed to the surface of the hollow silicon sphere in contact with the solution during application, so the cycle stability is relatively low. Difference.
  • Patent CN102211012A discloses a lithium ion sieve mixed matrix membrane with polyvinylidene fluoride as the binder, N,N-dimethylacetamide as the solvent and Li 1.6 Mn 1.6 O 4 as the core material for seawater extraction. Lithium, however, the core material loading per unit mass is small, the adsorption equilibrium time is long (in 12 hours), and the lithium extraction efficiency is low.
  • Patent CN109225121A discloses a hollow fiber membrane with polyacrylonitrile as a binder and H 1.6 Mn 1.6 O 4 as the core material. Although the lithium extraction efficiency has been further improved, it is caused by disproportionation during the elution of hydrochloric acid. Manganese dissolution loss is relatively serious, cycle stability is poor, and the corresponding supporting membrane modules are easily contaminated, and the maintenance cost of membrane equipment is expensive, which is not conducive to large-scale industrial operations.
  • the purpose of the present invention is to provide a fibrous spinning composite adsorption material with simple preparation process, high adsorption capacity, fast adsorption speed, easy large-scale preparation and industrial operation, and realizes low lithium concentration (5-30 mg/L) and low mineral content.
  • the efficient separation and recovery of lithium from liquid lithium ore resources of chemical degree lays the foundation for the industrial application of porous spinning composite adsorption materials.
  • a preparation method of a porous spinning composite material the steps are as follows:
  • the high molecular polymer is dissolved in the organic solvent by heating and stirring, and the mixed solution is allowed to stand at room temperature for defoaming;
  • step (2) adding a certain amount of lithium ion sieve powder and water-soluble porogen to the mixed solution obtained in step (1), and fully stirring and mixing to obtain a composite spinning dope of high molecular polymer/lithium ion sieve;
  • step (3) adding the composite spinning stock solution obtained in the step (2) into the raw material tank of the wet spinning equipment, and spraying the spinning stock solution into a coagulation bath through a spinneret to carry out phase inversion molding to obtain a porous composite precursor;
  • step (3) Carrying out drawing and washing of the solidified composite strand in step (3), and after curing, a porous composite lithium ion screen spinning fiber is obtained.
  • step (4) The porous composite lithium ion sieve spinning fiber obtained in step (4) is applied to the extraction of lithium from liquid lithium ore.
  • the high molecular polymer is polyethylene, polypropylene, polyvinyl chloride, polyvinylidene fluoride, polytetrafluoroethylene, polystyrene, polyacrylonitrile, polyamide, polysulfone, sulfonated polysulfone, polyarylsulfone , One or more mixtures of polyethersulfone.
  • the organic solvent is one or a mixture of two or more selected from dimethylformamide, dimethylacetamide, dimethylsulfoxide, N-methylpyrrolidone, tetrahydrofuran, dichloromethane, and tetrachloromethane.
  • the lithium ion sieve powder is LiTi 2 O 4 , Li 2 TiO 3 , Li 4 Ti 5 O 12 , or a mixture of one or more of the H-type products thereof after acid washing.
  • the water-soluble porogen is one of LiCl, KCl, NaHCO 3 , (NH 4 ) 2 CO 3 , NH 4 HCO 3 , polyethylene glycol-200/400/600/800/1000, polyvinylpyrrolidone one or a mixture of two or more.
  • the added amount of the porogen is 2-10% of the total mass of the mixed solution. Under this condition, the porosity of the composite fiber can be greatly improved, and the lithium ion sieve powder material can be guaranteed not to leak.
  • the mass ratio of the high molecular polymer to the lithium ion sieve is 1:4-4:1.
  • the spinneret hole number of the wet spinning equipment is 20-60 holes
  • the spinneret hole diameter is 0.05-0.5mm
  • the spinneret speed is 2-20m/min
  • the winder speed is 2-30m/min.
  • the coagulation bath is a mixed aqueous solution containing one or more of the organic solvents dimethylformamide, dimethylacetamide, dimethylsulfoxide, N-methylpyrrolidone, tetrahydrofuran, and dichloromethane.
  • the mass fraction is 5-25%, and under this condition, the spinning fiber of the porous composite lithium ion sieve can be rapidly formed.
  • the invention also protects the application of the porous spinning composite material in the extraction of lithium from liquid lithium ore.
  • the liquid lithium ore is geothermal water, its salinity TDS is 1-10 g/L, the lithium-containing concentration is 5-30 mg/L, and the pH of the porous spinning composite material when lithium is extracted from geothermal water is controlled to be 7 -13;
  • the liquid lithium ore is low salinity salt lake surface brine, and the pH of the porous spinning composite material when lithium is extracted from the low salinity salt lake surface brine is controlled to be 7-13.
  • the porous spinning liquid lithium ore also includes salt lake brine, underground brine, mine brine, geothermal water, seawater, and submarine hydrothermal ore.
  • the method used by composite materials to extract lithium from liquid lithium ore includes adsorption column, adsorption bed and adsorption tower operation.
  • the porous spinning composite material of the present invention not only has a simple preparation process and low cost, but also has mature supporting equipment, which is easy for large-scale production and application of the material.
  • the porous spinning composite material of the present invention effectively solves the problems of poor fluidity, difficulty in molding, poor stability, difficulty in recycling and difficulty in large-scale production of lithium ion sieve powder materials.
  • the porous spinning composite material of the present invention has good selectivity for lithium ions, high adsorption capacity, adsorption rate and cycle stability, and can be widely used in different types of liquid lithium ore, especially The separation and extraction of lithium in geothermal water, and the supporting lithium extraction method is easy to realize continuous industrial operation.
  • Figure 1(a) is a physical diagram of the polysulfone-H 2 TiO 3 porous spinning composite material prepared in Example 1 of the present invention
  • Figure 1(b) is an enlarged view of a polarizing microscope of the polysulfone-H 2 TiO 3 porous spinning composite material prepared in Example 1 of the present invention
  • Figure 2(a) is a comparison diagram of the adsorption capacity of the polysulfone-H 2 TiO 3 porous spinning composite prepared in Example 1 of the present invention and powder H 2 TiO 3 under the same conditions for adsorbing lithium;
  • Figure 2(b) is a comparison diagram of the cycle stability of the polysulfone-H 2 TiO 3 porous spinning composite prepared in Example 1 of the present invention and powder H 2 TiO 3 under the same conditions for lithium adsorption;
  • Figure 3(a) is a physical diagram of the polyacrylonitrile-H 4 Ti 5 O 12 porous spinning composite material prepared in Example 2 of the present invention
  • Figure 3(b) is an enlarged view of a polarizing microscope of the polyacrylonitrile-H 4 Ti 5 O 12 porous spinning composite material prepared in Example 2 of the present invention
  • Fig. 4 (a) is the actual picture of the polyacrylonitrile-Li 2 TiO 3 porous spinning composite material prepared in Example 3 of the present invention
  • Figure 4(b) is an enlarged view of a polarizing microscope of the polyacrylonitrile-Li 2 TiO 3 porous spinning composite material prepared in Example 3 of the present invention.
  • H 2 TiO 3 powder and 8g water-soluble porogen PEG-400 weigh 10g H 2 TiO 3 powder and 8g water-soluble porogen PEG-400 into the above-mentioned polysulfone mixed solution, fully mix and stir evenly, so that H-type lithium ion sieve powder H 2 TiO 3 is uniformly dispersed in the polysulfone mixed solution middle.
  • the prepared porous polysulfone-H 2 TiO 3 composite spinning material was applied to the geothermal water with an initial lithium ion concentration of 26.5895 mg ⁇ L -1 for lithium extraction, and the pH of the geothermal water was adjusted to 12.1. 1 g of polysulfone - H2TiO3 porous spinning composite was added for adsorption.
  • Figure 1(a) and Figure 1(b) for the physical image and magnified image of the prepared material by polarized light microscope, and Figure 2(a) for the comparison of the adsorption capacity and cycle stability of the as-prepared material for Li adsorption under the same conditions as that of powder H 2 TiO 3 . and Figure 2(b). It can be seen that the lithium ion sieve powder coated with the spinning fiber can still maintain a high adsorption capacity and rate, and there is no significant decrease compared with the powder material.
  • the fibrous spinning composite adsorption material prepared in this example has greatly improved adsorption rate and adsorption capacity compared with adsorption materials such as granular and film.
  • adsorption materials such as granular and film.
  • the PVC-LiMn 2 O 4 granular composite adsorbent disclosed in the patent CN101898113A and the PVC-Li 1.6 Mn 1.6 O 4 film composite adsorbent disclosed in the patent CN102211012A the time for reaching the adsorption equilibrium at room temperature is 120 hours and 8 hours, while the porous polysulfone-H 2 TiO 3 spinning composite prepared in this example only needs 1 hour to reach the adsorption equilibrium at room temperature.
  • porous PVC-PEG-H 2 TiO 3 composite microspheres reported in the document "ACS Applied Materials & Interfaces, 2019, 11(29), 26364-26372", although the adsorption rate has been further improved, the adsorption can be achieved within 3 hours Equilibrium, but the adsorption capacity is low, only 7 mg ⁇ g -1 , while the porous polysulfone-H 2 TiO 3 spinning composite prepared in this example can reach 23.39 mg ⁇ g -1 , and the adsorption equilibrium time is only 40 minutes , the adsorption performance was significantly improved.
  • the prepared polyacrylonitrile/H 4 Ti 5 O 12 spinning composite was applied to geothermal water for lithium extraction, the pH of the geothermal water was adjusted to 11.8, and 1 g of polysulfone-H 2 TiO 3 was added to 1.5 L of geothermal water for porous spinning.
  • the adsorption capacity of silk composite material can reach 20.07mg/g, and the adsorption equilibrium can be reached in 50 minutes.
  • Li 2 TiO 3 powder 10 g was weighed and added to the above polyacrylonitrile mixed solution, fully mixed and stirred evenly, so that the lithium ion sieve powder was uniformly dispersed in the polyacrylonitrile mixed solution.
  • the adsorption rate of the polyacrylonitrile-Li 2 TiO 3 spinning composite material prepared in this example is significantly improved.
  • the polyacrylonitrile-Li 2 TiO 3 electrospinning nanofiber membrane reported in the document "Journal of Industrial and Engineering Chemistry, 2019, 70, 124-135", which has an initial lithium ion concentration of 70 mg ⁇ L -1 In the lithium chloride solution, the adsorption equilibrium was reached in 12 hours at room temperature, and the equilibrium adsorption capacity was 28 mg ⁇ g -1 .
  • the polyacrylonitrile-Li 2 TiO 3 spinning composite material has a column bed dynamic adsorption capacity of 29.8 mg ⁇ g -1 under the same adsorption conditions, and the adsorption equilibrium time is only 1 hour, and the efficiency is increased by 12 times. ; At the same time, the spinning composite material is easier to process than the nanofiber membrane, has high strength, and is easy to be applied in engineering.

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Abstract

本发明公开了一种多孔纺丝复合材料的方法及其提锂应用，方法包括如下步骤：(1)将高分子聚合物与有机溶剂混合加热搅拌，使其充分溶解，并静置脱泡；(2)向该混合溶液中加入锂离子筛粉末及水溶性致孔剂，充分搅拌混合均匀；(3)利用湿法纺丝设备将混合溶液喷丝至凝固浴中相转化成型；(4)通过牵伸水洗，烘干固化后得到多孔纺丝复合吸附材料。将获得的多孔纺丝复合吸附材料应用于液体锂矿中锂的提取。本发明不仅有效地解决了粉体材料的流动性和循环稳定性差的问题，而且相对于粒状、棒状等吸附材料而言，其吸附速率和吸附容量得到了极大的提升，因而在盐湖卤水、地下卤水、地热水等中锂资源的开发利用方面具有良好的应用前景。

Description

一种多孔纺丝复合材料的制备方法及其提锂应用 技术领域
本发明属于材料化工领域，涉及锂离子吸附材料，尤其是一种多孔纺丝复合材料的方法。
背景技术
锂，作为最轻的金属，广泛的应用于航空航天、锂离子电池、核工业、陶瓷、电子器件等领域，被誉为21世纪的“战略性能源金属”。随着现代高新科技的不断发展，人们对锂的需求量日益剧增。锂的来源主要分为两类：一是以锂云母、锂辉石、透锂长石等为主的固体锂矿资源，二是以盐湖卤水、浓海水、地热水、地下卤水等为主的液体锂矿资源。但随着固体锂矿资源的日益枯竭及提取时较高的能耗，人们逐渐将目光转向了储量丰富、成本较低的液体锂矿资源。
目前，在液体锂矿中提取锂的方法主要有沉淀法、电化学法、萃取法、吸附法等，其中吸附法具有成本低、工艺简单、绿色高效的优势，逐渐成为最具有应用前景的提锂方法。该技术的关键是制备吸附性能优异的锂吸附剂，而锂离子筛型氧化物因其具有较高的吸附容量和锂离子选择性，逐渐成为研究的热点。但锂离子筛型氧化物大多以超细粉末形式存在，较差的流动性和循环稳定性极大的限制了其在工业上的应用，解决该问题的关键是制备一种吸附容量高、吸附速率快、循环稳定性好、成本低的复合锂离子筛吸附剂。
通过检索，发现如下相关专利文献报道：
1、专利CN101898113A公开了一种以聚氯乙烯为粘结剂，锰系锂离子筛(LMO：LiMn 2O 4、Li 1.6Mn 1.6O 4、Li 4Mn 5O 12)为内核材料的球形锂离子复合吸附剂，虽然流动性差的问题得到了改善，但经包覆后的锂离子筛吸附速率下降明显。
2、专利CN106902781B公开了一种负载HMO的介孔空心硅球，其拥有较大的比表面积和吸附速率，但应用时锂离子筛直接暴露于空心硅球表面与溶液接触，因此循环稳定性较差。
3、专利CN102211012A公开了一种以聚偏氟乙烯为粘结剂，N,N-二甲基乙酰胺为溶剂、Li 1.6Mn 1.6O 4为内核材料的锂离子筛混合基质膜用于海水提锂，然而单位质量的内核材料负载量少，吸附平衡时间长(以12小时计)，提锂效率较低。
4、专利CN109225121A公开了一种以聚丙烯腈为粘结剂，H 1.6Mn 1.6O 4为内 核材料的中空纤维膜，虽然提锂效率得到了进一步提升，但在盐酸洗脱时由于歧化反应造成锰溶损较为严重，循环稳定性较差，且相应配套膜组件易被污染，膜设备维护费用昂贵，不利于规模化工业操作。
由于地热水锂矿矿化度低，一般仅1～10g/L、含锂浓度低(5～30mg/L)，其绿色高效提取困难；另一方面，对于低矿化度的盐湖湖表卤水，由于锰系锂离子筛溶损，既易造污染，且循环稳定性差，上述专利提到的吸附材料不适用于地热水和低矿化度的盐湖湖表卤水提取锂。
为实现从液体锂矿中绿色高效的提取锂，需开发一种制备工艺简单、性能稳定、吸附效率高、易于工业化操作的多孔纺丝复合吸附剂。
发明内容
本发明目的在于提供一种制备流程简单、吸附容量高、吸附速度快、易于规模化制备和工业化操作的纤维状纺丝复合吸附材料，实现含锂浓度低(5～30mg/L)和低矿化度的液体锂矿资源中高效的分离回收锂，为多孔纺丝复合吸附材料的工业化应用奠定基础。
一种多孔纺丝复合材料的制备方法，步骤如下：
(1)将高分子聚合物加热搅拌溶解于有机溶剂中，并将混合溶液在室温下静置脱泡；
(2)向步骤(1)中获得的混合溶液中加入一定量的锂离子筛粉末及水溶性致孔剂，并充分搅拌混合均匀，获得高分子聚合物/锂离子筛的复合纺丝原液；
(3)将步骤(2)中获得的复合纺丝原液加入湿法纺丝设备的原料罐中，通过喷丝头将纺丝原液喷入凝固浴中进行相转化成型，获得多孔复合原丝；
(4)将步骤(3)中凝固成型的复合原丝进行牵伸洗涤，经固化后获得多孔复合锂离子筛纺丝纤维。
(5)将步骤(4)中获得的多孔复合锂离子筛纺丝纤维应用于液体锂矿中锂的提取。
而且所述高分子聚合物为聚乙烯、聚丙烯、聚氯乙烯、聚偏氟乙烯、聚四氟乙烯、聚苯乙烯、聚丙烯腈、聚酰胺、聚砜、磺化聚砜、聚芳砜、聚醚砜中的一种或两种以上的混合物。
而且所述有机溶剂为二甲基甲酰胺、二甲基乙酰胺、二甲基亚砜、N-甲基吡 咯烷酮、四氢呋喃、二氯甲烷、四氯甲烷中的一种或两种以上的混合物。
而且所述锂离子筛粉末为所述锂离子筛粉末为LiTi 2O 4、Li 2TiO 3、Li 4Ti 5O 12，或其酸洗后H型产物中一种或两种以上的混合物。
而且所述水溶性致孔剂为LiCl、KCl、NaHCO 3、(NH 4) 2CO 3、NH 4HCO 3、聚乙二醇-200/400/600/800/1000、聚乙烯吡咯烷酮中的一种或两种以上的混合物。
而且所述致孔剂的添加量为混合溶液总质量的2～10％，此条件下可较大程度提高复合纤维的孔隙率，且保证锂离子筛粉末材料不发生泄露。
而且所述高分子聚合物与锂离子筛的质量比为1:4～4:1。
而且所述湿法纺丝设备喷丝头孔数为20-60孔，喷丝孔直径为0.05～0.5mm，喷丝速度为2-20m/min，收卷机速度为2-30m/min。
而且所述凝固浴为含有机溶剂二甲基甲酰胺、二甲基乙酰胺、二甲基亚砜、N-甲基吡咯烷酮、四氢呋喃、二氯甲烷中一种或两中以上的混合水溶液，其质量分数为5～25％，此条件下可使多孔复合锂离子筛纺丝纤维快速成型。
本发明还保护多孔纺丝复合材料在液体锂矿中提取锂中的应用。
所述的液体锂矿为地热水，其矿化度TDS为1～10g/L、含锂浓度为5～30mg/L，多孔纺丝复合材料在地热水提取锂时的pH控制为7-13；
所述的液体锂矿为低矿化度的盐湖湖表卤水，多孔纺丝复合材料在低矿化度的盐湖湖表卤水提取锂时的pH控制为7-13。
所述多孔纺丝所述液体锂矿还包括盐湖卤水、地下卤水、井矿卤水、地热水、海水、海底热液矿。
复合材料在液体锂矿中提取锂时所用的方法包括吸附柱、吸附床和吸附塔式操作。
本发明的优点和积极效果是：
(1)本发明的一种多孔纺丝复合材料不仅制备工艺流程简单、成本低，而且配套设备成熟，易于材料的规模化生产和应用。
(2)本发明的一种多孔纺丝复合材料有效地解决了锂离子筛粉末材料流动性差、成型困难、稳定性差、难以回收利用和规模化生产困难的问题。
(3)本发明的一种多孔纺丝复合材料对于锂离子具有很好的选择性，具有较高的吸附容量、吸附速率和循环稳定性，可广泛的应用于不同类型液体锂矿，尤 其是地热水中锂的分离提取，且配套提锂方法易于实现连续工业化操作。
附图说明
图1(a)为本发明实施例1中制备的聚砜-H 2TiO 3多孔纺丝复合材料的实物图；
图1(b)为本发明实施例1中制备的聚砜-H 2TiO 3多孔纺丝复合材料的偏光显微镜放大图；
图2(a)为本发明实施例1中制备的聚砜-H 2TiO 3多孔纺丝复合材料与粉末H 2TiO 3在相同条件下吸附锂的吸附容量对比图；
图2(b)为本发明实施例1中制备的聚砜-H 2TiO 3多孔纺丝复合材料与粉末H 2TiO 3在相同条件下吸附锂的循环稳定性对比图；
图3(a)为本发明实施例2中制备的聚丙烯腈-H 4Ti 5O 12多孔纺丝复合材料的实物图；
图3(b)为本发明实施例2中制备的聚丙烯腈-H 4Ti 5O 12多孔纺丝复合材料的偏光显微镜放大图；
图4(a)为本发明实施例3中制备的聚丙烯腈-Li 2TiO 3多孔纺丝复合材料的实物图；
图4(b)为本发明实施例3中制备的聚丙烯腈-Li 2TiO 3多孔纺丝复合材料的偏光显微镜放大图。
具体实施方式
下面结合附图和具体实施例对本发明做进一步说明。
实施例1：聚砜-H 2TiO 3多孔纺丝复合材料的制备及其地热水提锂
称取10g聚砜颗粒于烧杯中，向烧杯中加入90g的N-甲基吡咯烷酮，使用恒温水浴磁力搅拌器加热搅拌，直至聚砜颗粒完全溶解。
称取10g H 2TiO 3粉末及8g水溶性致孔剂PEG-400加入到上述聚砜混合溶液中，充分混合搅拌均匀，使H型锂离子筛粉末H 2TiO 3均匀分散于聚砜混合溶液中。
将聚砜/H 2TiO 3复合纺丝原液加至湿法纺丝设备的原料罐中，调节喷丝头孔数为40，喷丝孔直径为0.07mm，喷丝速度为13m/min，牵伸收卷速度为16m/min，通过喷丝头喷丝到凝固浴中，经转相成型，牵伸水洗，获得多孔聚砜 -H 2TiO 3复合纺丝材料。此条件下获得的复合纺丝材料形貌完整，粗细均匀，吸附性能优异，相比于相同条件下喷丝孔直径为0.1mm获得的复合纺丝材料，吸附容量提升13.69％，吸附速率提升30％。
将制备的多孔聚砜-H 2TiO 3复合纺丝材料应用于锂离子初始浓度为26.5895mg·L -1的地热水中进行提锂，调节地热水pH为12.1，在1L地热水加入1g聚砜-H 2TiO 3多孔纺丝复合材料进行吸附。
所制备材料的实物图和偏光显微镜放大图见图1(a)及图1(b)，与粉末H 2TiO 3在相同条件下吸附锂的吸附容量对比及循环稳定性见图2(a)及图2(b)。可见，经纺丝纤维包覆成型后的锂离子筛粉末，仍可保持较高的吸附容量和速率，与粉末材料相比无明显降低。
本实施例中制备的纤维状纺丝复合吸附材料相对于粒状、膜状等吸附材料而言，其吸附速率和吸附容量得到了极大的提升。例如专利CN101898113A中公开的PVC-LiMn 2O 4粒状复合吸附剂和专利CN102211012A中公开的PVC-Li 1.6Mn 1.6O 4膜状复合吸附剂，其在常温下达到吸附平衡的时间分别为120小时和8小时，而本实施例中制备的多孔聚砜-H 2TiO 3纺丝复合材料在常温下仅需要1小时即可达到吸附平衡。例如文献“ACS Applied Materials & Interfaces，2019，11(29)，26364-26372”中报道的多孔PVC-PEG-H 2TiO 3复合微球，虽吸附速率得到了进一步提升，3小时即可达到吸附平衡，但吸附容量较低，仅为7mg·g -1，而本实施例中制备的多孔聚砜-H 2TiO 3纺丝复合可达23.39mg·g -1，且吸附平衡时间仅40分钟，各项吸附性能均得到显著提升。
实施例2：聚丙烯腈-H 4Ti 5O 12纺丝复合材料的制备及其地热水提锂
称取10g聚丙烯腈粉末于烧杯中，向烧杯中加入90g的二甲基甲酰胺，使用恒温水浴磁力搅拌器加热搅拌，直至聚丙烯腈粉末完全溶解。
称取5g H 4Ti 5O 12粉末加入到上述聚丙烯腈混合溶液中，充分混合搅拌均匀，使锂离子筛粉末均匀分散于聚丙烯腈混合溶液中。
将聚丙烯腈/H 4Ti 5O 12复合纺丝原液加至湿法纺丝设备的原料罐中，调节喷丝头孔数为50，喷丝孔直径为0.05mm，喷丝速度为10m/min，牵伸收卷速度为110m/min，通过喷丝头喷丝到凝固浴中，经转相成型，牵伸水洗，获得聚丙烯腈-H 4Ti 5O 12纺丝复合材料。所得材料的实物图及偏光显微镜放大图见图3(a) 及图3(b)。
将制备的聚丙烯腈/H 4Ti 5O 12纺丝复合材料应用于地热水提锂，调节地热水pH为11.8，在1.5L地热水加入1g聚砜-H 2TiO 3多孔纺丝复合材料进行吸附，吸附容量可达20.07mg/g，50分钟即可达到吸附平衡。
实施例3：聚丙烯腈-Li 2TiO 3纺丝复合材料的制备及其地热水提锂
称取10.5g聚丙烯腈粉末于烧杯中，向烧杯中加入90g的二甲基甲酰胺，使用恒温水浴磁力搅拌器加热搅拌，直至聚丙烯腈粉末完全溶解。
称取10g Li 2TiO 3粉末加入到上述聚丙烯腈混合溶液中，充分混合搅拌均匀，使锂离子筛粉末均匀分散于聚丙烯腈混合溶液中。
将聚丙烯腈/Li 2TiO 3复合纺丝原液加至湿法纺丝设备的原料罐中，调节喷丝头孔数为40，喷丝孔直径为0.07mm，喷丝速度为10m/min，牵伸收卷速度为10m/min，通过喷丝头喷丝到凝固浴中，经转相成型，牵伸水洗，获得聚丙烯腈-Li 2TiO 3纺丝复合材料，并经进一步酸洗后获得聚丙烯腈-H 2TiO 3纺丝复合材料。并在上述地热水中进行吸附，控制吸附pH为12，吸附柱的半径为5cm，柱高为50cm，流速为20ml·min -1。所得材料的实物图及偏光显微镜放大图见图4(a)及图4(b)。
本实施例中制备的聚丙烯腈-Li 2TiO 3纺丝复合材料相比于聚丙烯腈-Li 2TiO 3静电纺丝纳米纤维膜吸附速率得到了显著提升。例如文献“Journal of Industrial and Engineering Chemistry，2019，70，124-135”中报道的聚丙烯腈-Li 2TiO 3静电纺丝纳米纤维膜，其在初始锂离子初始浓度为70mg·L -1的氯化锂溶液中，常温下12小时达到吸附平衡，平衡吸附容量为28mg·g -1。而本实施例中聚丙烯腈-Li 2TiO 3纺丝复合材料，在相同吸附条件下，其柱床动态吸附容量达29.8mg·g -1，且吸附平衡时间仅1小时，效率提高12倍；同时，纺丝复合材料比纳米纤维膜更易加工，强度大、易于工程化应用。
以上显示和描述了本发明的实施例，均体现了本发明的制备简单、原料廉价易得等优点。应当理解的是，优选实施例对本发明的技术方案进行的详细说明是示意性而非限制性的，本领域技术人员在阅读本发明说明书的基础上，可以根据上述说明加以改进或变换，例如在材料制备过程中无需添加制孔剂，获得强度更高的吸附材料，所有这些改进和变换都应属于本发明所附权利要求的保护范围。

Claims (10)

  1. 一种多孔纺丝复合材料的制备方法，其特征在于，步骤如下：
    (1)将高分子聚合物加热搅拌溶解于有机溶剂中，并将混合溶液在室温下静置脱泡；
    (2)向步骤(1)中获得的混合溶液中加入一定量的锂离子筛粉末及水溶性致孔剂，并充分搅拌混合均匀，获得高分子聚合物/锂离子筛的复合纺丝原液；
    (3)将步骤(2)中获得的复合纺丝原液加入湿法纺丝设备的原料罐中，通过喷丝头将纺丝原液喷入凝固浴中进行相转化成型，获得多孔纺丝复合原材料；
    (4)将步骤(3)中凝固成型的复合原丝进行牵伸洗涤，经固化后获得多孔纺丝复合材料。
  2. 根据权利要求1所述的方法，其特征在于：所述高分子聚合物为聚乙烯、聚丙烯、聚氯乙烯、聚偏氟乙烯、聚四氟乙烯、聚苯乙烯、聚丙烯腈、聚酰胺、聚砜、磺化聚砜、聚芳砜、聚醚砜中的一种或两种以上的混合物。
  3. 根据权利要求1所述的方法，其特征在于：所述有机溶剂为二甲基甲酰胺、二甲基乙酰胺、二甲基亚砜、N-甲基吡咯烷酮、四氢呋喃、二氯甲烷中的一种或两种以上的混合物。
  4. 根据权利要求1所述的方法，其特征在于：所述锂离子筛粉末为LiTi 2O 4、Li 2TiO 3、Li 4Ti 5O 12，或其酸洗后H型产物中一种或两种以上的混合物。
  5. 根据权利要求1所述的方法，其特征在于：所述水溶性致孔剂为LiCl、KCl、NaHCO 3、NH 4HCO 3、聚乙二醇-200/400/600/800/1000、聚乙烯吡咯烷酮中的一种或两种以上的混合物。
  6. 根据权利要求1所述的方法，其特征在于：所述致孔剂的添加量为混合溶液总质量的2～10％，所述高分子聚合物与锂离子筛的质量比为1:4～4:1。
  7. 根据权利要求1所述的方法，其特征在于：所述湿法纺丝设备喷丝头孔数为20-60孔，喷丝孔直径为0.05～0.5mm，喷丝速度为2-20m/min，收卷机速度为2-30m/min。
  8. 根据权利要求1所述的方法，其特征在于：所述凝固浴为含有机溶剂二甲基甲酰胺、二甲基乙酰胺、二甲基亚砜、N-甲基吡咯烷酮、四氢呋喃、二氯甲烷中一种或两中以上的混合水溶液，其质量分数为5～25％。
  9. 一种根据权利要求1-8任一权利要求方法制备得到的多孔纺丝复合材料 在液体锂矿中提取锂的应用。
  10. 根据权利要求9所述的应用，其特征在于：所述的液体锂矿为地热水，其矿化度TDS为1～10g/L、含锂浓度为5～30mg/L，多孔纺丝复合材料在地热水提取锂时的pH控制为7-13；或所述的液体锂矿为低矿化度的盐湖湖表卤水，多孔纺丝复合材料在低矿化度的盐湖湖表卤水提取锂时的pH控制为7-13。
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Cited By (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN115701807A (zh) * 2022-11-08 2023-02-14 北京碧水源膜科技有限公司 一种锂离子筛H2TiO3吸附帘式膜的制备方法及应用所述帘式膜的盐湖提锂系统
CN115845825A (zh) * 2022-11-29 2023-03-28 北京碧水源膜科技有限公司 一种锂吸附剂的制备方法及实现所述方法的设备
CN116116370A (zh) * 2022-12-14 2023-05-16 北京碧水源膜科技有限公司 具有高吸附容量和高吸附速率的钛系锂吸附剂的制备方法
CN116272851A (zh) * 2023-02-16 2023-06-23 西安金藏膜环保科技有限公司 一种用于锂离子提取的沸石负载型复合材料的制备方法
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WO2024126603A1 (en) * 2022-12-14 2024-06-20 Watercycle Technologies Limited Material
WO2024170619A1 (en) * 2023-02-15 2024-08-22 Watercycle Technologies Limited Method of forming absorptive hollow fiber membranes using solvent of dimethyl isosorbide
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CN119320492A (zh) * 2023-07-17 2025-01-17 中国石油化工股份有限公司 含锂离子筛的聚酰胺材料和分离膜及它们的制备方法

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
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CN115970661B (zh) * 2023-01-30 2024-09-20 江苏海普功能材料有限公司 一种高吸附量的锂离子印迹纳米复合颗粒的制备方法
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WO2025129574A1 (zh) * 2023-12-21 2025-06-26 广东邦普循环科技有限公司 一种双层锂离子筛纤维材料及其制备方法和应用
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Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101898113A (zh) 2010-08-11 2010-12-01 华东理工大学 球形二氧化锰型锂离子筛
CN102211012A (zh) 2010-09-10 2011-10-12 中国海洋大学 一种锂离子筛膜及其制备方法
CN106902781A (zh) 2017-03-08 2017-06-30 江苏大学 改性介孔空心硅球吸附剂的制备方法及其应用
CN109225121A (zh) 2018-08-27 2019-01-18 石河子大学 复合吸附剂的制备方法和卤水提锂方法
CN110090614A (zh) * 2019-05-28 2019-08-06 湖南大学 一种锂离子筛吸附剂的制备方法及其产品与应用
US20190275473A1 (en) * 2018-03-08 2019-09-12 Ut-Battelle, Llc Lithium extraction composite for recovery of lithium from brines, and process of using said composition

Family Cites Families (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP6692530B2 (ja) * 2016-03-31 2020-05-13 国立大学法人信州大学 チタン酸系リチウム吸着剤の製造方法
CN106622170A (zh) * 2016-12-21 2017-05-10 江苏大学 一种锂钛型离子筛复合膜的制备方法及其用途
KR102146063B1 (ko) * 2018-08-22 2020-08-20 명지대학교 산학협력단 H2TiO3가 함침된 복합나노시트를 포함하는 리튬흡착제 및 그 제조방법
CN109537106B (zh) * 2018-11-09 2021-05-18 中国科学院山西煤炭化学研究所 高速干喷纺丝制备异形截面碳纤维前驱体纤维、预氧化纤维或碳纤维的方法
CN109289754A (zh) * 2018-11-14 2019-02-01 天津科技大学 一种磷钼酸铵复合凝胶吸附材料的制备方法
CN110975795A (zh) * 2019-12-20 2020-04-10 南京工业大学 一种提锂吸附剂的合成方法

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101898113A (zh) 2010-08-11 2010-12-01 华东理工大学 球形二氧化锰型锂离子筛
CN102211012A (zh) 2010-09-10 2011-10-12 中国海洋大学 一种锂离子筛膜及其制备方法
CN106902781A (zh) 2017-03-08 2017-06-30 江苏大学 改性介孔空心硅球吸附剂的制备方法及其应用
US20190275473A1 (en) * 2018-03-08 2019-09-12 Ut-Battelle, Llc Lithium extraction composite for recovery of lithium from brines, and process of using said composition
CN109225121A (zh) 2018-08-27 2019-01-18 石河子大学 复合吸附剂的制备方法和卤水提锂方法
CN110090614A (zh) * 2019-05-28 2019-08-06 湖南大学 一种锂离子筛吸附剂的制备方法及其产品与应用

Non-Patent Citations (3)

* Cited by examiner, † Cited by third party
Title
ACS APPLIED MATERIALS & INTERFACES, vol. 11, no. 29, 2019, pages 26364 - 26372
JOURNAL OF INDUSTRIAL AND ENGINEERING CHEMISTRY, vol. 70, 2019, pages 124 - 135
See also references of EP4209266A4

Cited By (14)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
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CN115845825A (zh) * 2022-11-29 2023-03-28 北京碧水源膜科技有限公司 一种锂吸附剂的制备方法及实现所述方法的设备
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WO2024170619A1 (en) * 2023-02-15 2024-08-22 Watercycle Technologies Limited Method of forming absorptive hollow fiber membranes using solvent of dimethyl isosorbide
CN116272851A (zh) * 2023-02-16 2023-06-23 西安金藏膜环保科技有限公司 一种用于锂离子提取的沸石负载型复合材料的制备方法
CN116351380A (zh) * 2023-03-21 2023-06-30 郑州大学 一种低成本层状锂离子筛及其制备方法和应用
CN116351380B (zh) * 2023-03-21 2024-04-12 郑州大学 一种低成本层状锂离子筛及其制备方法和应用
CN119320492A (zh) * 2023-07-17 2025-01-17 中国石油化工股份有限公司 含锂离子筛的聚酰胺材料和分离膜及它们的制备方法
CN116966866A (zh) * 2023-07-31 2023-10-31 上海科技大学 一种具有光热辅助提锂功能的非织造材料、制备方法及应用
CN116966866B (zh) * 2023-07-31 2025-11-14 上海科技大学 一种具有光热辅助提锂功能的非织造材料、制备方法及应用
CN118892809A (zh) * 2024-06-28 2024-11-05 山东大学 一种二维碳材料修饰的锂离子筛复合膜及其制备方法

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