CN112661193B - Method for simultaneously preparing binary and ternary high-performance composite aerogel by using iron tailings - Google Patents
Method for simultaneously preparing binary and ternary high-performance composite aerogel by using iron tailings Download PDFInfo
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- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 title claims abstract description 88
- 239000004964 aerogel Substances 0.000 title claims abstract description 68
- 229910052742 iron Inorganic materials 0.000 title claims abstract description 44
- 239000002131 composite material Substances 0.000 title claims abstract description 40
- 238000000034 method Methods 0.000 title claims abstract description 31
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 claims abstract description 42
- 239000011240 wet gel Substances 0.000 claims abstract description 37
- 239000007788 liquid Substances 0.000 claims abstract description 29
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Chemical compound O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 28
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- 229910021641 deionized water Inorganic materials 0.000 claims abstract description 19
- 239000002904 solvent Substances 0.000 claims abstract description 19
- 239000011218 binary composite Substances 0.000 claims abstract description 16
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- 238000001035 drying Methods 0.000 claims abstract description 12
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- UQSXHKLRYXJYBZ-UHFFFAOYSA-N Iron oxide Chemical compound [Fe]=O UQSXHKLRYXJYBZ-UHFFFAOYSA-N 0.000 claims description 32
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- 239000000203 mixture Substances 0.000 claims description 14
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- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 claims description 10
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 claims description 9
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- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 claims description 6
- FEWJPZIEWOKRBE-UHFFFAOYSA-N Tartaric acid Natural products [H+].[H+].[O-]C(=O)C(O)C(O)C([O-])=O FEWJPZIEWOKRBE-UHFFFAOYSA-N 0.000 claims description 6
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- DKGAVHZHDRPRBM-UHFFFAOYSA-N Tert-Butanol Chemical compound CC(C)(C)O DKGAVHZHDRPRBM-UHFFFAOYSA-N 0.000 claims description 5
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- 239000003054 catalyst Substances 0.000 claims description 5
- GRYLNZFGIOXLOG-UHFFFAOYSA-N Nitric acid Chemical compound O[N+]([O-])=O GRYLNZFGIOXLOG-UHFFFAOYSA-N 0.000 claims description 4
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- 230000002378 acidificating effect Effects 0.000 claims description 3
- BRPQOXSCLDDYGP-UHFFFAOYSA-N calcium oxide Chemical compound [O-2].[Ca+2] BRPQOXSCLDDYGP-UHFFFAOYSA-N 0.000 claims description 3
- 239000000292 calcium oxide Substances 0.000 claims description 3
- ODINCKMPIJJUCX-UHFFFAOYSA-N calcium oxide Inorganic materials [Ca]=O ODINCKMPIJJUCX-UHFFFAOYSA-N 0.000 claims description 3
- 239000000395 magnesium oxide Substances 0.000 claims description 3
- CPLXHLVBOLITMK-UHFFFAOYSA-N magnesium oxide Inorganic materials [Mg]=O CPLXHLVBOLITMK-UHFFFAOYSA-N 0.000 claims description 3
- AXZKOIWUVFPNLO-UHFFFAOYSA-N magnesium;oxygen(2-) Chemical compound [O-2].[Mg+2] AXZKOIWUVFPNLO-UHFFFAOYSA-N 0.000 claims description 3
- 239000000843 powder Substances 0.000 claims description 3
- 235000012239 silicon dioxide Nutrition 0.000 claims description 3
- FEWJPZIEWOKRBE-JCYAYHJZSA-N Dextrotartaric acid Chemical compound OC(=O)[C@H](O)[C@@H](O)C(O)=O FEWJPZIEWOKRBE-JCYAYHJZSA-N 0.000 claims description 2
- 150000007513 acids Chemical class 0.000 claims description 2
- TWNQGVIAIRXVLR-UHFFFAOYSA-N oxo(oxoalumanyloxy)alumane Chemical compound O=[Al]O[Al]=O TWNQGVIAIRXVLR-UHFFFAOYSA-N 0.000 claims description 2
- CHWRSCGUEQEHOH-UHFFFAOYSA-N potassium oxide Chemical compound [O-2].[K+].[K+] CHWRSCGUEQEHOH-UHFFFAOYSA-N 0.000 claims description 2
- 229910001950 potassium oxide Inorganic materials 0.000 claims description 2
- KKCBUQHMOMHUOY-UHFFFAOYSA-N sodium oxide Chemical compound [O-2].[Na+].[Na+] KKCBUQHMOMHUOY-UHFFFAOYSA-N 0.000 claims description 2
- 229910001948 sodium oxide Inorganic materials 0.000 claims description 2
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- 238000002360 preparation method Methods 0.000 abstract description 16
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- XUIMIQQOPSSXEZ-UHFFFAOYSA-N Silicon Chemical compound [Si] XUIMIQQOPSSXEZ-UHFFFAOYSA-N 0.000 abstract description 9
- 239000003513 alkali Substances 0.000 abstract description 9
- 229910052710 silicon Inorganic materials 0.000 abstract description 9
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- RBTBFTRPCNLSDE-UHFFFAOYSA-N 3,7-bis(dimethylamino)phenothiazin-5-ium Chemical compound C1=CC(N(C)C)=CC2=[S+]C3=CC(N(C)C)=CC=C3N=C21 RBTBFTRPCNLSDE-UHFFFAOYSA-N 0.000 abstract description 7
- 229960000907 methylthioninium chloride Drugs 0.000 abstract description 7
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- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 description 6
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- BOTDANWDWHJENH-UHFFFAOYSA-N Tetraethyl orthosilicate Chemical compound CCO[Si](OCC)(OCC)OCC BOTDANWDWHJENH-UHFFFAOYSA-N 0.000 description 3
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- 238000010586 diagram Methods 0.000 description 3
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- CSDREXVUYHZDNP-UHFFFAOYSA-N alumanylidynesilicon Chemical compound [Al].[Si] CSDREXVUYHZDNP-UHFFFAOYSA-N 0.000 description 2
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Abstract
Description
技术领域technical field
本发明涉及一种以铁尾矿为原料同时制备二元和三元复合气凝胶的方法,属于气凝胶的制备领域。The invention relates to a method for simultaneously preparing binary and ternary composite aerogels by using iron tailings as raw materials, and belongs to the field of aerogel preparation.
背景技术Background technique
SiO2气凝胶是一种由纳米级二氧化硅颗粒组合而成的一种具有三维网状多孔结构的纳米材料,具有较高的比表面积,极低的密度,和较低的常温热导率,在保温隔热、吸附、CO2隔离、催化剂载体、航空航天等等很多领域都有良好的应用前景。二氧化硅气凝胶的主要制备工艺通常包括溶胶凝胶和干燥两个典型步骤,分别用以形成并最大限度保持凝胶三维结构,从而最终获得气凝胶产品,目前公认的成熟工艺通常以正硅酸乙酯(TEOS)为硅源经过超临界干燥获得二氧化硅气凝胶,但其在技术以及应用方面仍存在很多挑战,例如TEOS硅源价格较高,而超临界干燥设备要求严苛,技术难度大,不利于大范围工业化推广,因此,为了克服上述缺点,寻找更廉价的硅源和更简便的干燥方式现实意义重大。 SiO2 aerogel is a nanomaterial with a three-dimensional network porous structure composed of nano-scale silica particles, with high specific surface area, extremely low density, and low room temperature thermal conductivity. It has good application prospects in many fields such as thermal insulation, adsorption, CO 2 isolation, catalyst carrier, aerospace and so on. The main preparation process of silica aerogel usually includes two typical steps of sol-gel and drying, which are respectively used to form and maximize the three-dimensional structure of the gel, so as to finally obtain aerogel products. Ethyl orthosilicate (TEOS) is a silicon source to obtain silica aerogel through supercritical drying, but there are still many challenges in technology and application, such as the high price of TEOS silicon source, and the strict requirements of supercritical drying equipment. Therefore, in order to overcome the above shortcomings, it is of great practical significance to find a cheaper silicon source and a simpler drying method.
铁尾矿是选矿后的废弃物,是工业固体废弃物的主要组成部分。目前,我国的尾矿综合利用率只有7%,堆存的铁尾矿量高达十几亿吨,占全部尾矿堆存总量的近1/3。因此,铁尾矿的综合回收利用问题已受到全社会的广泛关注。一般而言,铁尾矿中主要以二氧化硅,氧化铝,氧化铁、氧化镁和氧化钙的含量最多,其余为少量的伴生元素氧化物,目前对于铁尾矿的利用主要在尾矿再选、矿区采空区填充、尾矿建筑材料、土壤改良剂等方面,这些方法虽然可以在数量上解决部分尾矿堆存的问题,但在相关更具市场竞争力的高附加值产品方面仍然有待研究和推广,这不利于铁尾矿的资源化高效利用。铁尾矿中的二氧化硅是天然的硅源,经过碱处理后即可提取作为制备高附加值二氧化硅气凝胶的原料,在实现绿色生态发展的同时又可以提升铁尾矿综合利用效率。同时,尾矿中的氧化铝和氧化铁同样是制备气凝胶的潜在原料,通常这些有价元素含量相对较低,单独提纯或利用涉及工艺复杂、成本高,因此本发明提出将其作为必要组分保留在气凝胶中,与二氧化硅复合制备复合气凝胶,起到协同增益功能化的效果。目前利用尾矿中的二氧化硅制备气凝胶的相关报道目前较少,公开号CN108658130A公开了一种从铁尾矿同时制备氧化铁和二氧化硅气凝胶的方法,该方法包括酸洗提铁和碱熔提硅以分别获得铁源和硅源,但并未将二者合并制备复合材料的问题解决;公开号CN109133072A公开了一种以铁尾矿为原料超快速制备疏水二氧化硅气凝胶的方法,公开号CN109012517A公开了一种以铁尾矿为原料制备复合型硅基气凝胶的方法,上述方法虽然通过碱熔的工艺在一定程度上获得了氧化铝和二氧化硅的复合材料,但由于初始碱熔处理温度较低,氧化铁仍在滞留于碱熔渣中,无法将尾矿中的氧化铁提出制备氧化铁/二氧化硅气凝胶复合材料。Iron tailings are wastes after beneficiation and are the main component of industrial solid wastes. At present, the comprehensive utilization rate of tailings in my country is only 7%, and the stockpiled iron tailings amount to more than one billion tons, accounting for nearly 1/3 of the total tailings stockpiled. Therefore, the comprehensive recovery and utilization of iron tailings has been widely concerned by the whole society. Generally speaking, the content of silica, alumina, iron oxide, magnesium oxide and calcium oxide in iron tailings is the largest, and the rest are a small amount of associated element oxides. At present, the utilization of iron tailings is mainly in tailings recycling In terms of beneficiation, goaf filling in mining areas, tailings building materials, soil conditioners, etc., although these methods can solve some of the tailings stockpiling problems quantitatively, they are still related to more market-competitive high value-added products. It needs to be studied and promoted, which is not conducive to the efficient utilization of iron tailings. Silica in iron tailings is a natural source of silicon. After alkali treatment, it can be extracted as a raw material for the preparation of high value-added silica aerogels, which can improve the comprehensive utilization of iron tailings while achieving green ecological development. efficiency. At the same time, alumina and iron oxide in the tailings are also potential raw materials for the preparation of aerogels. Usually, the content of these valuable elements is relatively low, and separate purification or utilization involves complicated processes and high costs. Therefore, the present invention proposes to use them as necessary. The components remain in the aerogel and are compounded with silica to prepare a composite aerogel, which has the effect of synergistic gain functionalization. There are few reports on the preparation of aerogel by using silica in tailings. Publication No. CN108658130A discloses a method for simultaneously preparing iron oxide and silica aerogel from iron tailings. The method includes pickling Iron extraction and alkali melting extraction of silicon are used to obtain iron source and silicon source respectively, but the problem of combining the two to prepare composite materials is not solved; Publication No. CN109133072A discloses an ultra-fast preparation of hydrophobic silica using iron tailings as raw material The method of aerogel, publication number CN109012517A discloses a method for preparing composite silicon-based aerogel with iron tailings as raw material, although the above method obtains alumina and silica to a certain extent through the process of alkali melting However, due to the low initial alkali melting temperature, the iron oxide is still retained in the alkali slag, and the iron oxide in the tailings cannot be extracted to prepare the iron oxide/silica aerogel composite material.
发明内容SUMMARY OF THE INVENTION
针对现有技术中存在的技术问题,本发明要解决的技术问题在于提供一种利用铁尾矿同时制备二元和三元高性能复合气凝胶的方法,以固体废弃物铁尾矿为原料,价格低廉、来源广泛,制备条件温和、工艺简单、设备要求低,易于实现业化制备,可以同时获得二元复合气凝胶和三元磁性复合气凝胶。所制备的气凝胶的振实密度小于0.20g/cm3平均孔径为5.25-8.67nm,其中二元复合气凝胶的比表面积可达到986m2/g,可以作为优良的载体催化剂,三元磁性复合气凝胶比表面积可达到600m2/g,对亚甲基蓝的吸附量超过300mg/g,吸附性能优良且容易分离,二者均具有良好的应用潜力。In view of the technical problems existing in the prior art, the technical problem to be solved by the present invention is to provide a method for simultaneously preparing binary and ternary high-performance composite aerogels by using iron tailings, using solid waste iron tailings as raw materials , low price, wide source, mild preparation conditions, simple process, low equipment requirements, easy to realize industrial preparation, and can simultaneously obtain binary composite aerogel and ternary magnetic composite aerogel. The tap density of the prepared aerogel is less than 0.20g/ cm3 , and the average pore size is 5.25-8.67nm, and the specific surface area of the binary composite aerogel can reach 986m2 /g, which can be used as an excellent carrier catalyst. The specific surface area of the magnetic composite aerogel can reach 600m 2 /g, the adsorption capacity of methylene blue is more than 300mg/g, the adsorption performance is excellent and the separation is easy, both of which have good application potential.
为解决上述技术问题,本发明采取的技术方案为:In order to solve the above-mentioned technical problems, the technical scheme adopted in the present invention is:
利用铁尾矿同时制备二元和三元高性能复合气凝胶的方法,包括如下步骤:(1)以铁尾矿为原料,与粉体氢氧化钠均匀混合后,置于马弗炉中,加热保温反应完全后冷却至室温,将得到的混合物用去离子水冲洗4-10次并收集洗液;(2)将步骤(1)中得到的洗液置于容器中静置10-60分钟直至洗液明显分层,用吸管吸出上层清液,分别向上层清液和下层混合液中加入酸性催化剂,并分别调节洗液pH至9-10.5,静置直至块状凝胶形成后,将凝胶分别取出置于去离子水中继续老化12-24小时得到湿凝胶,老化过程中更换去离子水3-6次;(3)将步骤(2)获得的湿凝胶分别置于置换剂溶液中12-24小时进行溶剂置换,期间每2-6小时更换新鲜置换剂溶液,以完全除去湿凝胶中的水和其他残留试剂;(4)将步骤(3)溶剂置换完成后的湿凝胶分别取出,进行常压干燥,即可获得所述的二元复合气凝胶和三元磁性复合气凝胶。The method for simultaneously preparing binary and ternary high-performance composite aerogels from iron tailings includes the following steps: (1) using iron tailings as raw materials, uniformly mixing with powdered sodium hydroxide, and placing them in a muffle furnace , cooling to room temperature after the heating and heat preservation reaction is completed, the obtained mixture is rinsed with deionized water for 4-10 times and the washing liquid is collected; (2) the washing liquid obtained in step (1) is placed in a container and allowed to stand for 10-60 until the washing liquid is clearly stratified, suck out the supernatant liquid with a pipette, add an acidic catalyst to the upper supernatant liquid and the mixed liquid of the lower layer respectively, and adjust the pH of the washing liquid to 9-10.5 respectively, and let stand until the massive gel is formed. The gels are respectively taken out and placed in deionized water to continue aging for 12-24 hours to obtain wet gels, and the deionized water is replaced 3-6 times during the aging process; (3) the wet gels obtained in step (2) are placed in replacement Perform solvent replacement in the solvent solution for 12-24 hours, and replace the fresh replacement agent solution every 2-6 hours to completely remove water and other residual reagents in the wet gel; (4) Replace the solvent replacement in step (3) with the The wet gels are respectively taken out and dried under normal pressure to obtain the binary composite aerogel and the ternary magnetic composite aerogel.
铁尾矿为粉末状,粒度50目以上,含有二氧化硅、氧化铝、氧化铁、氧化镁、氧化钙、氧化钾和氧化钠。Iron tailings are in powder form with a particle size of more than 50 mesh, and contain silicon dioxide, aluminum oxide, iron oxide, magnesium oxide, calcium oxide, potassium oxide and sodium oxide.
步骤(1)中,铁尾矿与氢氧化钠的质量比为1:1-3,冷却后的混合物每次冲洗用水量,为混合物质量与水的体积的比为1:20-100(克/毫升),操作温度为室温。In step (1), the mass ratio of iron tailings and sodium hydroxide is 1:1-3, and the water consumption of each rinse of the mixture after cooling is 1:20-100 (grams) for the ratio of the mass of the mixture to the volume of water. /ml), the operating temperature is room temperature.
步骤(1)中加热温度为700-900℃,保温时间为1-5小时。In step (1), the heating temperature is 700-900° C., and the holding time is 1-5 hours.
步骤(2)中,所用的酸性催化剂为上层清液选用磷酸、硝酸、盐酸、硫酸或柠檬酸溶液催化凝胶,所用酸溶液的质量分数为2-15%,下层混合液选用磷酸、硝酸、盐酸、硫酸或柠檬酸溶液搭配纯酒石酸或纯抗坏血酸催化凝胶,所用酸溶液的质量分数为2-15%,酒石酸、抗坏血酸与其他酸的质量比为1:1-1:5。In step (2), the acid catalyst used is that the supernatant liquid selects phosphoric acid, nitric acid, hydrochloric acid, sulfuric acid or citric acid solution catalytic gel, the mass fraction of the acid solution used is 2-15%, and the lower layer mixed solution selects phosphoric acid, nitric acid, Hydrochloric acid, sulfuric acid or citric acid solution is combined with pure tartaric acid or pure ascorbic acid to catalyze the gel, the mass fraction of the acid solution used is 2-15%, and the mass ratio of tartaric acid, ascorbic acid and other acids is 1:1-1:5.
步骤(3)中,所用的置换剂为乙醇、叔丁醇、丙酮、甲醇、乙二醇中的一种或几种,每次用量为至少完全浸没湿凝胶。In step (3), the used displacer is one or more selected from ethanol, tert-butanol, acetone, methanol, and ethylene glycol, and the dosage for each time is to at least completely immerse the wet gel.
步骤(3)中常压干燥的方法是将湿凝胶放于敞口容器中,用保鲜膜密封,在保鲜膜上开孔5-30个,孔大小为1x1mm,以便在干燥过程中调控湿凝胶的干燥速率,减少凝胶骨架坍塌,最后将容器置于烘箱中在50-150℃条件下烘干24-72小时至湿凝胶完全干燥。The method of atmospheric drying in step (3) is to put the wet gel in an open container, seal it with a plastic wrap, and open 5-30 holes on the plastic wrap, and the hole size is 1×1 mm, so as to control the humidity during the drying process. The drying rate of the gel can reduce the collapse of the gel skeleton. Finally, the container is placed in an oven and dried at 50-150 ° C for 24-72 hours until the wet gel is completely dry.
步骤(4)所获得的二元复合气凝胶和三元磁性复合气凝胶的振实密度为0.158-0.194g/cm3,比表面积为320-986m2/g,平均孔径为5.25-8.67nm,二者对于典型染料亚甲基蓝的吸附能力分别可达到322mg/g和354mg/g。The tap density of the binary composite aerogel and the ternary magnetic composite aerogel obtained in step (4) is 0.158-0.194 g/cm 3 , the specific surface area is 320-986 m 2 /g, and the average pore size is 5.25-8.67 nm, the adsorption capacity of the two for the typical dye methylene blue can reach 322 mg/g and 354 mg/g, respectively.
本发明的有益效果在于:The beneficial effects of the present invention are:
1、本发明仅以铁尾矿为原料,具有来源广泛、价格低廉、绿色环保无毒的优势,符合国家节能减排的发展要求,同时利用铁尾矿中自有的氧化铁、氧化铝同步实现复合材料的制备,获得具有高比表面积,高吸附性能的硅铝及硅铝铁复合气凝胶,有效提升了产品的功能性和附加值。1. The present invention only uses iron tailings as raw materials, has the advantages of wide source, low price, green environmental protection and non-toxicity, meets the development requirements of national energy conservation and emission reduction, and simultaneously utilizes the own iron oxide and alumina in iron tailings. The preparation of composite materials is realized, and silicon-aluminum and silicon-aluminum-iron composite aerogels with high specific surface area and high adsorption performance are obtained, which effectively improves the functionality and added value of the product.
2、本发明通过高温碱熔处理,使铁尾矿中氧化铁向铁酸盐进行有效转化,实现了难溶铁向可溶铁的转变,再通过简单的溶胶凝胶工艺、静置分层、溶剂置换和常压干燥处理,一步获得了铝硅二元复合气凝胶和铝硅铁三元磁性复合气凝胶,同时,利用氧化铝和氧化铁对二氧化硅气凝胶协同增强,硅铝二元复合气凝胶孔结构发达,比表面积可达到986m2/g,亚甲基蓝吸附量超过300mg/g,而硅铝铁三元磁性复合气凝胶虽然比表面积稍低,但其比表面积也可超过600m2/g,氧化铁的催化氧化作用使得其对亚甲基蓝的吸附能力接近甚至高于硅铝二元复合气凝胶,超过350mg/g,体现出了优良的吸附潜能,同时经过溶胶凝胶过程和有机酸的还原作用,三元磁性复合气凝胶中的氧化铁具有磁性,主要以磁性γ氧化铁形态存在,无需额外添加磁性物质,一步实现了尾矿中铁源的磁性功能化,使得三元磁性复合气凝材料更易于分离。2. The present invention effectively converts iron oxide in iron tailings to ferrite through high-temperature alkali melting treatment, and realizes the conversion of insoluble iron to soluble iron. , solvent replacement and drying at atmospheric pressure to obtain Al-Si binary composite aerogel and Al-Si-Fe ternary magnetic composite aerogel in one step. At the same time, silica aerogel is synergistically enhanced by alumina and iron oxide. The silicon-alumina binary composite aerogel has a well-developed pore structure, the specific surface area can reach 986m 2 /g, and the adsorption capacity of methylene blue exceeds 300mg/g. It can also exceed 600m 2 /g. The catalytic oxidation of iron oxide makes its adsorption capacity for methylene blue close to or even higher than that of silicon-aluminum binary composite aerogel, exceeding 350mg/g, showing excellent adsorption potential. The gelation process and the reduction effect of organic acids, the iron oxide in the ternary magnetic composite aerogel is magnetic, mainly exists in the form of magnetic γ iron oxide, without the need to add additional magnetic substances, one-step realization of the magnetic functionalization of the iron source in the tailings , making the ternary magnetic composite aerogel material easier to separate.
3、本发明所用工艺,无需额外硅源,无需离子交换,无需表面改性,无需超临界干燥,无需磁性添加剂,仅以铁尾矿中的有效成分实现气凝胶自体复合增强,制备条件简单温和,设备要求低,能耗小,节能环保的同时也为固废资源的利用提出了新的思路,易于工业化生产。3. The process used in the present invention requires no additional silicon source, no ion exchange, no surface modification, no supercritical drying, and no magnetic additives. Only the effective components in the iron tailings are used to achieve self-composite reinforcement of aerogels, and the preparation conditions are simple. Mild, low equipment requirements, low energy consumption, energy saving and environmental protection, it also puts forward new ideas for the utilization of solid waste resources, and is easy to industrialize production.
附图说明Description of drawings
图1为本发明的工艺流程图;Fig. 1 is the process flow diagram of the present invention;
图2为实施例3洗液静置分层效果图;Fig. 2 is embodiment 3 lotion standing and layering effect diagram;
图3为实施例3三元磁性复合气凝胶(左)和二元复合气凝胶实物图;Fig. 3 is embodiment 3 ternary magnetic composite aerogel (left) and binary composite aerogel physical map;
图4为实施例3三元磁性复合气凝胶磁性展示图;Fig. 4 is the magnetic display diagram of embodiment 3 ternary magnetic composite aerogel;
图5为实施例3复合气凝胶SEM-EDS图;5 is a SEM-EDS image of the composite aerogel of Example 3;
图6为实施例3复合气凝胶XRD图谱;Fig. 6 is embodiment 3 composite aerogel XRD pattern;
图7为实施例3复合气凝胶氮气吸附等温线。7 is the nitrogen adsorption isotherm of the composite aerogel of Example 3.
具体实施方式Detailed ways
下面通过具体实施方式来进一步说明本发明的技术方案。本领域技术人员应该明了,所述实施例仅仅是帮助理解本发明,不应视为对本发明的具体限制。The technical solutions of the present invention are further described below through specific embodiments. It should be understood by those skilled in the art that the embodiments are only for helping the understanding of the present invention, and should not be regarded as a specific limitation of the present invention.
实施例1Example 1
一种利用铁尾矿同时制备二元和三元高性能复合气凝胶的方法,具体制备步骤如下:(1)将50目以上的粉末状铁尾矿与粉体氢氧化钠按质量比1:1放入坩埚中并混合均匀,将坩埚放入马弗炉中,设置马弗炉升温速率为5℃/min,加热至700℃后保温4小时得到铁尾矿与氢氧化钠反应后的混合物,将反应后的混合物与去离子水按固体质量与液体体积比1:20冲洗4次得到洗液。A method for simultaneously preparing binary and ternary high-performance composite aerogels by utilizing iron tailings, the specific preparation steps are as follows: (1) powdered iron tailings with a size of more than 50 meshes and powdered sodium hydroxide in a mass ratio of 1 : 1 Put it into the crucible and mix it evenly, put the crucible into the muffle furnace, set the heating rate of the muffle furnace to be 5 ℃/min, heat it to 700 ℃ and keep it for 4 hours to obtain the iron tailings and sodium hydroxide after the reaction. The mixture was washed four times with deionized water at a solid mass to liquid volume ratio of 1:20 to obtain a washing solution.
(2)将洗液在静置30分钟后明显分层,吸取上层清液至其他玻璃容器中。将质量分数为5%的盐酸+抗坏血酸(质量比2:1)分别加入两个容器中调节容器中液体至pH=9.1,静置两个容器中的液体直至形成块体凝胶。(2) After standing for 30 minutes, the lotion was obviously stratified, and the supernatant was drawn into other glass containers. Add 5% hydrochloric acid + ascorbic acid (mass ratio 2:1) into two containers respectively, adjust the liquid in the container to pH=9.1, and let the liquid in the two containers stand until a bulk gel is formed.
(3)将两个块体凝胶取出分别浸入去离子水中并在室温下静置16小时老化得到湿凝胶,期间更换3次去离子水。(3) The two bulk gels were taken out and immersed in deionized water respectively and aged at room temperature for 16 hours to obtain wet gels, during which the deionized water was replaced 3 times.
(4)将老化湿凝胶取出浸入90mL乙醇溶剂中静置20小时,期间更换3次溶剂,以完全去除湿凝胶孔隙中的水和残留试剂。(4) The aged wet gel was taken out and immersed in 90 mL of ethanol solvent for 20 hours, during which the solvent was replaced three times to completely remove water and residual reagents in the pores of the wet gel.
(5)将湿凝胶从置换溶剂中取出后置于500ml烧杯中,用保鲜膜将容器口封住并在保鲜膜上扎4个小洞,常压状态下将上层清液得到的湿凝胶在85℃并保持36小时干燥,下层混合液得到的湿凝胶在110℃保持36小时干燥,即可得到所述的二元复合气凝胶和三元磁性复合气凝胶。(5) Remove the wet gel from the replacement solvent and place it in a 500ml beaker, seal the mouth of the container with plastic wrap and tie 4 small holes in the plastic wrap, and wet the gel obtained from the supernatant under normal pressure. The gel is dried at 85° C. and kept for 36 hours, and the wet gel obtained from the lower mixed solution is kept at 110° C. for 36 hours to dry, and the binary composite aerogel and the ternary magnetic composite aerogel can be obtained.
实施例2Example 2
一种利用铁尾矿同时制备二元和三元高性能复合气凝胶的方法,具体制备步骤如下:(1)将50目以上的粉末状铁尾矿与粉体氢氧化钠按质量比1:2放入坩埚中并混合均匀,将坩埚放入马弗炉中,设置马弗炉升温速率为5℃/min,加热至780℃后保温3.5小时得到铁尾矿与氢氧化钠反应后的混合物,将反应后的混合物与去离子水按固体质量与液体体积比1:30冲洗6次得到洗液。A method for simultaneously preparing binary and ternary high-performance composite aerogels by utilizing iron tailings, the specific preparation steps are as follows: (1) powdered iron tailings with a size of more than 50 meshes and powdered sodium hydroxide in a mass ratio of 1 : 2 Put it into the crucible and mix it evenly, put the crucible into the muffle furnace, set the heating rate of the muffle furnace to be 5 ℃/min, heat to 780 ℃ and keep the temperature for 3.5 hours to obtain the iron tailings and sodium hydroxide after the reaction. The mixture was washed 6 times with deionized water at a solid mass to liquid volume ratio of 1:30 to obtain a washing solution.
(2)洗液在静置40分钟后明显分层,吸取上层清液至其他玻璃容器中。将质量分数为5%的硫酸+抗坏血酸(质量比2:1)分别加入两个容器中调节容器中液体至pH=9.3,静置两个容器中的液体直至形成块体凝胶。(2) After standing for 40 minutes, the lotion is obviously stratified, and the supernatant is drawn into other glass containers. The mass fraction of 5% sulfuric acid + ascorbic acid (mass ratio 2:1) was added to the two containers respectively to adjust the liquid in the container to pH=9.3, and the liquid in the two containers was allowed to stand until a bulk gel was formed.
(3)将两个块体凝胶取出分别浸入去离子水中并在室温下静置20小时老化得到湿凝胶,期间更换4次去离子水。(3) The two bulk gels were taken out and immersed in deionized water respectively and aged at room temperature for 20 hours to obtain wet gels, during which the deionized water was replaced 4 times.
(4)将老化湿凝胶取出浸入100mL甲醇溶剂中静置22小时,期间更换5次溶剂,以完全去除湿凝胶孔隙中的水和残留试剂。(4) The aged wet gel was taken out and immersed in 100 mL of methanol solvent for 22 hours, during which the solvent was replaced 5 times to completely remove water and residual reagents in the pores of the wet gel.
(5)将湿凝胶从置换溶剂中取出后置于500ml烧杯中,用保鲜膜将烧杯口封住并在保鲜膜上扎8个小洞,常压状态下将上层清液得到的湿凝胶在80℃保持48小时干燥,下层混合液得到的湿凝胶在120℃保持48小时干燥,即可得到所述的二元复合气凝胶和三元磁性复合气凝胶。(5) Remove the wet gel from the replacement solvent and place it in a 500ml beaker, seal the mouth of the beaker with plastic wrap and poke 8 small holes on the plastic wrap, and wet the gel obtained from the supernatant under normal pressure. The gel is kept dry at 80° C. for 48 hours, and the wet gel obtained from the lower mixed solution is kept at 120° C. for 48 hours to dry, and the binary composite aerogel and the ternary magnetic composite aerogel can be obtained.
实施例3Example 3
一种利用铁尾矿同时制备二元和三元高性能复合气凝胶的方法,具体制备步骤如下:(1)将50目以上的粉末状铁尾矿与粉体氢氧化钠按质量比1:2.5放入坩埚中并混合均匀,将坩埚放入马弗炉中,设置马弗炉升温速率为5℃/min,加热至850℃后保温3小时得到铁尾矿与氢氧化钠反应后的混合物,将反应后的混合物与去离子水按固体质量与液体体积比1:40冲洗8次得到洗液。A method for simultaneously preparing binary and ternary high-performance composite aerogels by utilizing iron tailings, the specific preparation steps are as follows: (1) powdered iron tailings with a size of more than 50 meshes and powdered sodium hydroxide in a mass ratio of 1 : 2.5 Put it into the crucible and mix it evenly, put the crucible into the muffle furnace, set the heating rate of the muffle furnace to be 5 ℃/min, heat it to 850 ℃ and keep it for 3 hours to obtain the iron tailings and sodium hydroxide after the reaction. The mixture was washed 8 times with deionized water at a solid mass to liquid volume ratio of 1:40 to obtain a washing solution.
(2)洗液在静置50分钟后明显分层,吸取上层清液至其他玻璃容器中,将质量分数为10%的磷酸+酒石酸(质量比3:1)分别加入两个容器中调节容器中液体pH=9.7,静置两个容器中的液体直至分布形成块体凝胶。(2) After standing for 50 minutes, the washing liquid is obviously layered, and the supernatant liquid is drawn into other glass containers, and phosphoric acid + tartaric acid (mass ratio 3:1) with a mass fraction of 10% is added to the two containers respectively. Medium liquid pH = 9.7, and the liquids in both containers were allowed to stand until the distribution formed a bulk gel.
(3)将两个块体凝胶取出分别浸入去离子水中并在室温下静置18小时老化得到湿凝胶,期间更换5次去离子水。(3) The two bulk gels were taken out and immersed in deionized water respectively and aged at room temperature for 18 hours to obtain wet gels, during which the deionized water was replaced 5 times.
(4)将老化湿凝胶取出浸入120mL乙二醇溶剂中静置24小时,期间更换7次溶剂,以完全去除湿凝胶孔隙中的水和残留试剂。(4) The aged wet gel was taken out and immersed in 120 mL of ethylene glycol solvent for 24 hours, during which the solvent was replaced 7 times to completely remove water and residual reagents in the pores of the wet gel.
(5)将湿凝胶从置换溶剂中取出后置于500ml烧杯中,用保鲜膜将烧杯口封住并在保鲜膜上扎12个小洞,常压状态下将上层清液得到的湿凝胶在75℃并保持60小时干燥,下层混合液得到的湿凝胶在120℃保持60小时干燥,即可得到所述的二元复合气凝胶和三元磁性复合气凝胶。(5) Take out the wet gel from the replacement solvent and place it in a 500ml beaker, seal the mouth of the beaker with plastic wrap and tie 12 small holes in the plastic wrap, and wet the gel obtained from the supernatant under normal pressure. The gel is dried at 75° C. and kept for 60 hours, and the wet gel obtained from the lower mixed solution is kept at 120° C. for 60 hours to dry, and the binary composite aerogel and the ternary magnetic composite aerogel can be obtained.
实施例4Example 4
一种利用铁尾矿同时制备二元和三元高性能复合气凝胶的方法,具体制备步骤如下:(1)将50目以上的粉末状铁尾矿与粉体氢氧化钠按质量比1:3放入坩埚中并混合均匀,将坩埚放入马弗炉中,设置马弗炉升温速率为5℃/min,加热至900℃后保温2.5小时得到铁尾矿与氢氧化钠反应后的混合物,将反应后的混合物与去离子水按固体质量与液体体积比1:50冲洗8次得到洗液。A method for simultaneously preparing binary and ternary high-performance composite aerogels by utilizing iron tailings, the specific preparation steps are as follows: (1) powdered iron tailings with a size of more than 50 meshes and powdered sodium hydroxide in a mass ratio of 1 : 3 put it into the crucible and mix it evenly, put the crucible into the muffle furnace, set the heating rate of the muffle furnace to be 5 ℃/min, heat it to 900 ℃ and keep it for 2.5 hours to obtain the iron tailings and sodium hydroxide after the reaction. The mixture is washed 8 times with deionized water at a solid mass to liquid volume ratio of 1:50 to obtain a washing solution.
(2)洗液在静置58分钟后明显分层,吸取上层清液至其他玻璃容器中。将质量分数为15%的柠檬酸+酒石酸(质量比3:1)分别加入两个容器中调节容器中液体pH=10.2,静置两个容器中的液体直至分布形成块体凝胶。(2) After standing for 58 minutes, the lotion was obviously stratified, and the supernatant was drawn into other glass containers. Add 15% citric acid + tartaric acid (mass ratio 3:1) into two containers respectively to adjust the pH of the liquid in the container to 10.2, and leave the liquid in the two containers to stand until the distribution forms a bulk gel.
(3)将两个块体凝胶取出分别浸入去离子水中并在室温下静置15小时老化得到湿凝胶,期间更换7次去离子水。(3) The two bulk gels were taken out and immersed in deionized water respectively and aged at room temperature for 15 hours to obtain wet gels, during which the deionized water was replaced 7 times.
(4)将老化湿凝胶取出浸入140mL叔丁醇溶剂中静置21小时,期间更换6次溶剂,以完全去除湿凝胶孔隙中的水和残留试剂。(4) The aged wet gel was taken out and immersed in 140 mL of tert-butanol solvent for 21 hours, during which the solvent was replaced 6 times to completely remove water and residual reagents in the pores of the wet gel.
(5)将湿凝胶从置换溶剂中取出后置500ml于烧杯中,用保鲜膜将烧杯口封住并在保鲜膜上扎18个小洞,常压状态下将上层清液得到的湿凝胶在70℃并保持72小时干燥,下层混合液得到的湿凝胶在130℃保持72小时干燥,即可得到所述的二元复合气凝胶和三元磁性复合气凝胶。(5) Take out the wet gel from the replacement solvent and place 500 ml in a beaker, seal the mouth of the beaker with plastic wrap and tie 18 small holes in the plastic wrap, and then wet the gel obtained from the supernatant under normal pressure. The gel is dried at 70° C. and kept for 72 hours, and the wet gel obtained from the lower mixed solution is kept at 130° C. for 72 hours to dry, and the binary composite aerogel and the ternary magnetic composite aerogel can be obtained.
表1Table 1
从表1可以得出,根据实际用酸性催化剂种类不同,产品的比表面积相差较多,这是由于酸的浓度和种类对二元复合气凝胶和三元磁性复合气凝胶的形成存在一定的影响,进而对胶体三围网络骨架结构的强度产生影响,中强酸催化作用下胶体的骨架结构比较完整,在干燥过程中配合表面张力小的置换剂,不会引起较大的骨架坍塌,从而保持良好的孔隙结构。对于三元磁性复合气凝胶而言,铁的存在会使得胶体在形成过程中由于氧化铁的掺杂而受到影响,导致最终气凝胶产品的比表面积降低,但氧化铁优异的催化氧化作用可以显著提升三元气凝胶对于亚甲基蓝染料的吸附净化作用,使得三元气凝胶在低比表面积的情况下仍然具有较高的亚甲基蓝吸附量,同时具有磁性易于分离,而可溶性铁盐前驱体在低温条件下难以生成,因此在碱熔阶段提升碱熔温度至700℃以上并适当增加NaOH配比是十分必要的。From Table 1, it can be concluded that the specific surface area of the product varies greatly according to the different types of acid catalysts actually used. This is because the concentration and type of acid have certain effects on the formation of binary composite aerogels and ternary magnetic composite aerogels. Under the catalysis of medium and strong acid, the skeleton structure of the colloid is relatively complete. In the drying process, the displacer with small surface tension will not cause a large skeleton to collapse, so as to maintain good pore structure. For the ternary magnetic composite aerogel, the presence of iron will make the colloid affected by the doping of iron oxide during the formation process, resulting in a decrease in the specific surface area of the final aerogel product, but the excellent catalytic oxidation effect of iron oxide It can significantly improve the adsorption and purification effect of ternary aerogel on methylene blue dye, so that the ternary aerogel still has a high adsorption capacity of methylene blue in the case of low specific surface area, and it is magnetic and easy to separate. It is difficult to generate under the conditions, so it is very necessary to increase the alkali melting temperature to above 700 °C and appropriately increase the NaOH ratio in the alkali melting stage.
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